JPS59222213A - Treatment of waste gas - Google Patents
Treatment of waste gasInfo
- Publication number
- JPS59222213A JPS59222213A JP58095288A JP9528883A JPS59222213A JP S59222213 A JPS59222213 A JP S59222213A JP 58095288 A JP58095288 A JP 58095288A JP 9528883 A JP9528883 A JP 9528883A JP S59222213 A JPS59222213 A JP S59222213A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- sox
- nox
- electron beam
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
Description
【発明の詳細な説明】
本発明は排ガスの処理方法に関する。より詳細(])
に述べると1本発明は窒素酸化物(以下”NOx”と略
記する場合がある)および/ま1こは硫黄酸化物(以下
°“SOx”と略記する場合がある)を含む排ガスにオ
ゾンおよびアルカリ性物質ケ添加させて電離性放射線欠
照射して排ガス乞処理する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating exhaust gas. In more detail (]), the present invention uses nitrogen oxides (hereinafter sometimes abbreviated as "NOx") and/or sulfur oxides (hereinafter sometimes abbreviated as "SOx"). The present invention relates to a method for treating exhaust gas by adding ozone and alkaline substances to exhaust gas and irradiating it with ionizing radiation.
1)、従来技術の説明
特開昭50−57064号は排ガスにアルカリ性物質例
えばアンモニアを添加することによって脱硝・脱硫の効
率を高める電子線照射による排ガスの処理方法馨開示し
ている。然しながうこの従来技術は、特に高い濃度のN
Oxおよび/まfこはSOXン含む4フ1ガス(例えば
石炭燃焼排ガス等)の脱硝・脱硫効率の点で改良される
べき課題を有している。1) Description of the Prior Art JP-A-50-57064 discloses a method for treating exhaust gas by electron beam irradiation, which improves the efficiency of denitrification and desulfurization by adding an alkaline substance such as ammonia to the exhaust gas. However, this conventional technique is particularly difficult to use when the concentration of N is high.
Ox and/or gases have problems that should be improved in terms of denitrification and desulfurization efficiency of four gases including SOX (for example, coal combustion exhaust gas, etc.).
発明の要約
従って1本発明の目的は、従来技術の課題乞解消し1こ
新規な排ガス処理方法ケ提供するととである。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a novel exhaust gas treatment method that overcomes the problems of the prior art.
本発明の特定的な目的はNOxおよび/又はSOxを含
む排ガスにオゾンおよびアルカリ性物質を添(2)
7JOさせ1こ状態で電離性改射線乞照射1−1窒素酸
化物および/または硫黄酸化物を固体生成物として同時
に除去せしめろことが出来る排ガスの処理方法欠提供す
ることである。A specific object of the present invention is to add ozone and alkaline substances to exhaust gas containing NOx and/or SOx (2) 7JO and irradiate the ionizing beam in this state with 1-1 nitrogen oxides and/or sulfur oxides. It is an object of the present invention to provide a method for treating exhaust gases that can simultaneously remove them as solid products.
本発明の他の目的および利点は添付図面と共に以下に一
層明らかにされる。Other objects and advantages of the invention will become more apparent below in conjunction with the accompanying drawings.
本発明の構成乞第1図欠参照して説明する。The structure of the present invention will be explained with reference to FIG. 1 (not shown).
生ず、第1図によってオゾン(03”l ならびにアル
カリ性物質を添加しない場合の説明乞する。第1図で排
出源」−から反応器−生に導入されたN(Jxおよび/
又はSOx Y含む排ガスは照射室λ内に配置し1こ電
子線照射装置灸からの電子線の照射を受ける。ここで排
ガスの主成分であるN2,0□、1+2C)の混合気体
は放射線化学反応によって、酸化性の強い活性種であろ
0原子、 UIIラジカル、 +(02ラジカル等を生
成し、これらの活性種によってN(JxおよびSOxは
酸化され、最終的には硝酸、1流酸ミストとなる。(下
記(1)および(2))
(3)
こうして生成されたミストは電気集塵器等の集塵装置J
により捕集され、排ガス中から除去される。このように
して、 NOxおよびSOxが除去さ才1て、浄化され
1こ排ガスはプロワー−φにより、煙突−tかも大気中
に故山される。Figure 1 shows the case in which ozone (03"l) and alkaline substances are not added. In Figure 1, N (Jx and/or
Alternatively, the exhaust gas containing SOx Y is placed in the irradiation chamber λ and is irradiated with an electron beam from a moxibustion electron beam irradiation device. Here, the mixed gas of N2, 0□, 1+2C), which is the main component of the exhaust gas, generates highly oxidizing active species such as 0 atoms, UII radicals, +(02 radicals, etc.) through radiation chemical reactions, and these active species Depending on the species, N (Jx and SOx) are oxidized and finally become nitric acid and first acid mist ((1) and (2) below) (3) The mist thus generated is collected by an electrostatic precipitator, etc. Dust equipment J
is collected and removed from the exhaust gas. In this way, NOx and SOx are removed and the purified exhaust gas is discharged into the atmosphere by the blower φ.
第1図で照射室の入[]手前に設けたオゾン添加口5か
ら03乞添加する事により、上記(]+ 、 (2+の
酸化反応乞促進しうる。この反応はNOxあるいはSO
xと0.との単純な酸化反応にとどまらず、電子線照射
によって生成した活生種(ラジカル等)も同時に反応に
寄与する点に特徴乞有する。このム二め添加口は必ず、
照射室の前に位置する必要がある。添加するオゾンの量
は処理するN□xの緻ならびKSOxの量に依存するが
、 NOxの濃度ならびにSOxの濃度の和以下で充分
である。しかし、オゾン濃度が高すぎるとオゾンによる
二次公害を引き(4)
おこすおそれがあり、−力任すぎるとオゾン添加の効果
が充分にあられれない。このため、添加するオゾンの量
は処理するNOxならびに3Hx濃度のI+
一〜−程度が望ましい。第1図で示すようにアル100
カリ性物質乞添加口Aから加える事により、 (11。By adding ozone from the ozone addition port 5 provided before entering the irradiation chamber in Fig. 1, the oxidation reaction of (]+ and (2+) can be accelerated.
x and 0. The unique feature of this method is that it not only involves a simple oxidation reaction with the electron beam, but also active species (radicals, etc.) generated by electron beam irradiation that also contribute to the reaction. This second addition port is sure to
It must be located in front of the irradiation chamber. The amount of ozone added depends on the density of N□x to be treated and the amount of KSOx, but it is sufficient that it is less than the sum of the NOx concentration and SOx concentration. However, if the ozone concentration is too high, there is a risk of secondary pollution caused by ozone (4), and if too much force is used, the effect of ozone addition may not be sufficiently achieved. For this reason, it is desirable that the amount of ozone added be about 1 to 1 - I+ of the NOx and 3Hx concentrations to be treated. As shown in Figure 1, by adding Al 100 from the addition port A, (11.
(2)で生成しタミスト等?中和し、固体生成物として
除去することができる。本発明の実施例ではアルカリ性
物質として、アンモニアガスを添加しているが、この場
合既に知られているように、アンモニアは電子線照射に
より反応性が高いラジカルを生成するので、IJi射線
化学反応乞促進すること。Generated by (2), Tamist etc.? It can be neutralized and removed as a solid product. In the embodiment of the present invention, ammonia gas is added as an alkaline substance, but in this case, as is already known, ammonia generates highly reactive radicals when irradiated with an electron beam, so it is difficult to react with IJi radiation chemical reactions. To promote.
まfこ気相反応なので反応速度が大きいことなどの点で
特に有効である。また、この添加[追よ、上述した放射
線化学反応がおこること、あるいは、電子線照射により
1粒子の生成速度の促進と帯電による捕集効率の向上な
どがおこり、集塵効率の向−ヒが見られるなどの利点が
あることから、照射室の前に設置することが望ましい。Since it is a gas phase reaction, it is particularly effective in that the reaction rate is high. In addition, this addition [additionally, the above-mentioned radiation chemical reaction occurs, or the electron beam irradiation accelerates the production rate of one particle and improves the collection efficiency due to charging, which improves the dust collection efficiency. It is desirable to install it in front of the irradiation room because it has the advantage of being visible.
ま1こ、アンモニアガスいる場合、アンモニアによるオ
ゾンの分解を極力抑えるTこめ、添加口は照射室直前で
あるこ(5)
とが望ましい。If ammonia gas is used, it is desirable that the addition port be located just before the irradiation chamber (5) to minimize the decomposition of ozone by ammonia.
却下に実施例および参考例乞掲げ本発明の構成および効
果乞より具体的に説明する。The structure and effects of the present invention will be explained more specifically by referring to examples and reference examples.
実施例 1〜2
石炭燃焼排ガス欠模擬したNO(60(1ppm)−S
O2(1000ppm)−ト120 (F3%)−0
2(i [lqら)−N2(ba l ance
)の混合ガスに、 270pr+mの濃度となる量
のオゾンならびに2600pp+nの濃度となる量のア
ンモニアを添加し、120℃でIMeVの電子線馨照射
し1こ時のNOxならびにSO2のa度を測定し1こ。Examples 1-2 NO (60 (1 ppm)-S) simulated lack of coal combustion exhaust gas
O2 (1000ppm) - 120 (F3%) -0
2(i[lq et al.)-N2(bal ance
) was added with ozone in an amount to give a concentration of 270 pr+m and ammonia in an amount to give a concentration of 2600 pp+n, and then irradiated with an IMeV electron beam at 120°C, and the degrees of NOx and SO2 at this time were measured. 1 piece.
この結果を第1表に示す。NOx濃度は4Mrad の
照射で600ppmから65ppm ヘ、まt、= 8
0. 濃度も10 [1[]ppmから50ppm以下
へといずれも初期a度の約10分の1から20分の1に
減少した。The results are shown in Table 1. The NOx concentration is 600 ppm to 65 ppm with 4 Mrad irradiation.
0. The concentration also decreased from 10 [1 [] ppm to 50 ppm or less, from about 1/10 to 1/20 of the initial a degree.
1 0.67 150 <502
4.0 65 <50(6)
実施例 3〜5.参考例 1〜2
実施例1および2と同じ条件で、電子線照射7行ない一
定時間に電気集塵器に捕集されfこ固体生成物の量乞測
定するとともに、この生成物ケ同定し1こ。この結果を
第2表の実施例ろ〜5に示ず。1 0.67 150 <502
4.0 65 <50 (6) Examples 3-5. Reference Examples 1 to 2 Under the same conditions as Examples 1 and 2, electron beam irradiation was performed 7 times, and the amount of solid product collected in an electrostatic precipitator was measured at a certain time, and this product was identified. child. The results are not shown in Examples 5 to 5 of Table 2.
まfここれと同じ混合ガスにオゾン添加をしなかった場
合について、同様の測定馨行なった。この結果を第6表
の参考例1〜2に示す。Similar measurements were conducted for the same mixed gas without the addition of ozone. The results are shown in Reference Examples 1 and 2 in Table 6.
これらの表かられかるように、捕集されfこ固体生成物
(硫酸アンモニウムと硝酸アンモニウムの混合物)の財
は、照射線量が大きいほど多く、ま1こオゾンン添加し
た場合は添加しない場合よりも捕集量が多くなっている
ことがわかる。例えば。As can be seen from these tables, the amount of collected solid product (a mixture of ammonium sulfate and ammonium nitrate) increases as the irradiation dose increases, and the amount of collected solid product (mixture of ammonium sulfate and ammonium nitrate) increases as the irradiation dose increases; It can be seen that the amount is increasing. for example.
実施例5は参考例2に比べ約50%の増加が見られる。Example 5 shows an increase of about 50% compared to Reference Example 2.
(7) 第2表 ろ OO 00(7) Table 2 RoOO 00
第1図は本発明の一態様Z示し1こフローシートである
。
C8)FIG. 1 is a flow sheet showing one embodiment of the present invention. C8)
Claims (1)
にオゾンならびにアルカリ性物質Z添加させた状態で電
離性放射線を照射し、窒素酸化物および/または硫黄酸
化物を固体生成物として同時に除去せしめることから成
る排ガスの処理方法。 2)添加するオゾンの量が、窒素酸化物ならびに硫黄酸
化物の#度の和に相当する址以下である特許請求の範囲
第1項記載の方法。 ろ)添加するアルカリ性物質の鑞が、窒素酸化物乞硝酸
として、硫黄酸化物を硫酸として、これを中和するに要
する量である特許請求の範囲第1項記載の方法。[Claims] 1) Exhaust gas containing nitrogen oxides and/or sulfur oxides 7 is irradiated with ionizing radiation in a state in which ozone and an alkaline substance Z are added to produce nitrogen oxides and/or sulfur oxides in solid form. A method of treating exhaust gas that consists of simultaneously removing it as a gas. 2) The method according to claim 1, wherein the amount of ozone added is equal to or less than the sum of the degrees of nitrogen oxides and sulfur oxides. 2) The method according to claim 1, wherein the alkaline substance added is in an amount necessary to neutralize nitrogen oxides and nitric acid and sulfur oxides as sulfuric acid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58095288A JPS59222213A (en) | 1983-05-30 | 1983-05-30 | Treatment of waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58095288A JPS59222213A (en) | 1983-05-30 | 1983-05-30 | Treatment of waste gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59222213A true JPS59222213A (en) | 1984-12-13 |
JPS6359729B2 JPS6359729B2 (en) | 1988-11-21 |
Family
ID=14133584
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58095288A Granted JPS59222213A (en) | 1983-05-30 | 1983-05-30 | Treatment of waste gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59222213A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63104635A (en) * | 1986-10-21 | 1988-05-10 | Japan Atom Energy Res Inst | Exhaust gas treatment by addition of ammonia and irradiation of radiant ray |
JPH0199633A (en) * | 1987-10-09 | 1989-04-18 | Mitsubishi Heavy Ind Ltd | Treatment of exhaust gas |
KR20000025341A (en) * | 1998-10-10 | 2000-05-06 | 이구택 | Method for removing nitrogen oxide by using ozone and ammonia |
KR100428841B1 (en) * | 1998-10-10 | 2004-08-06 | 주식회사 포스코 | Nitrogen oxide removal in low temperature plasma process using propylene and ozone |
KR100451690B1 (en) * | 1997-01-06 | 2004-11-20 | 인천광역시 | Method and apparatus for removing harmful compounds in exhaust gas by electron beam irradiation |
JP2013529545A (en) * | 2010-06-23 | 2013-07-22 | チャン,バオカン | Combustion exhaust gas purification and recycling system and method |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE8816695U1 (en) * | 1988-12-06 | 1990-05-03 | Mehler Vario System Gmbh, 6400 Fulda, De | |
DE8816696U1 (en) * | 1988-12-06 | 1990-05-03 | Mehler Vario System Gmbh, 6400 Fulda, De |
-
1983
- 1983-05-30 JP JP58095288A patent/JPS59222213A/en active Granted
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63104635A (en) * | 1986-10-21 | 1988-05-10 | Japan Atom Energy Res Inst | Exhaust gas treatment by addition of ammonia and irradiation of radiant ray |
JPH0521608B2 (en) * | 1986-10-21 | 1993-03-25 | Ebara Mfg | |
JPH0199633A (en) * | 1987-10-09 | 1989-04-18 | Mitsubishi Heavy Ind Ltd | Treatment of exhaust gas |
KR100451690B1 (en) * | 1997-01-06 | 2004-11-20 | 인천광역시 | Method and apparatus for removing harmful compounds in exhaust gas by electron beam irradiation |
KR20000025341A (en) * | 1998-10-10 | 2000-05-06 | 이구택 | Method for removing nitrogen oxide by using ozone and ammonia |
KR100428841B1 (en) * | 1998-10-10 | 2004-08-06 | 주식회사 포스코 | Nitrogen oxide removal in low temperature plasma process using propylene and ozone |
JP2013529545A (en) * | 2010-06-23 | 2013-07-22 | チャン,バオカン | Combustion exhaust gas purification and recycling system and method |
Also Published As
Publication number | Publication date |
---|---|
JPS6359729B2 (en) | 1988-11-21 |
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