JPS6044009B2 - Method for removing nitrogen oxides from exhaust gas - Google Patents
Method for removing nitrogen oxides from exhaust gasInfo
- Publication number
- JPS6044009B2 JPS6044009B2 JP52012686A JP1268677A JPS6044009B2 JP S6044009 B2 JPS6044009 B2 JP S6044009B2 JP 52012686 A JP52012686 A JP 52012686A JP 1268677 A JP1268677 A JP 1268677A JP S6044009 B2 JPS6044009 B2 JP S6044009B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- gas
- catalyst
- ammonia
- catalyst bed
- 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
Links
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title claims description 65
- 239000007789 gas Substances 0.000 title claims description 45
- 238000000034 method Methods 0.000 title claims description 21
- 239000003054 catalyst Substances 0.000 claims description 58
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 47
- 229910021529 ammonia Inorganic materials 0.000 claims description 13
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 5
- 230000007423 decrease Effects 0.000 claims description 5
- 239000000919 ceramic Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 238000002485 combustion reaction Methods 0.000 description 6
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical class N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 3
- 235000011130 ammonium sulphate Nutrition 0.000 description 3
- 231100000572 poisoning Toxicity 0.000 description 3
- 230000000607 poisoning effect Effects 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 1
- 230000009970 fire resistant effect Effects 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
【発明の詳細な説明】
本発明は排ガス中の窒素酸化物をアンモニア添加によ
り触媒床を用いて接触還元除去する排ガス中の窒素酸化
物の除去法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing nitrogen oxides from exhaust gas by catalytic reduction using a catalyst bed by adding ammonia.
火力発電所および各種工場より排出される燃焼排ガス
中には多量の窒素酸化物(NOx)が含まれており、大
気汚染の大きな要因として社会問題にもなつている。
この燃焼排ガス中に含まれる窒素酸化物を除去する方法
としては、大別して湿式法と乾式法の2通りがある。BACKGROUND OF THE INVENTION Combustion exhaust gas emitted from thermal power plants and various factories contains a large amount of nitrogen oxides (NOx), which has become a social problem as a major cause of air pollution.
There are two main methods for removing nitrogen oxides contained in this combustion exhaust gas: wet methods and dry methods.
しかしながら湿式法は装置が大型かつ複雑であり、価
格的にも非常に高価となり、しかも排液処理技術が充分
に確立されていないので、脱硝排液の処理に大きな問題
があるところから、最近は特に乾式法が注目されるよう
になつた。 乾式法による排ガス中の窒素酸化物の除去
法は、燃焼排ガス中にアンモニアガスを吹込み、耐火性
の触媒担体にり、Cr、Cu、TiO。However, the wet method requires large and complicated equipment, is very expensive, and the wastewater treatment technology has not been fully established, so there are major problems in treating the denitrification wastewater. In particular, the dry method has attracted attention. In the dry method for removing nitrogen oxides from exhaust gas, ammonia gas is blown into the combustion exhaust gas, and then Cr, Cu, and TiO are removed using a fire-resistant catalyst carrier.
、Fe等の触媒金属酸化物等の触媒物質を担持した触媒
床を用いて接触還元除去する方法である。 そして、従
来排ガス中の窒素酸化物をアンモニア添加により触媒床
を用いて接触還元除去する方法としては、例えば第1図
に示すとおり、燃焼排ガス中の管路1中に、枠2によつ
て包まれた粒状触媒3よりなる触媒床4を設置し、該触
媒床4の排ガス導入側前方流路にアンモニアガス導入口
5を配置し、管路1を通じて流れている燃焼排ガス6中
にアンモニアガス導入口5よりアンモニアを添加混合し
、触媒床4中で排ガス中の窒素酸化物を接触還元して無
害な窒素ガスとして大気中に放出する除去法が広く知ら
れている。This is a method of catalytic reduction removal using a catalyst bed supporting a catalytic material such as a catalytic metal oxide such as Fe. As a conventional method for removing nitrogen oxides in exhaust gas by catalytic reduction using a catalyst bed by adding ammonia, for example, as shown in FIG. A catalyst bed 4 made of granular catalyst 3 is installed, and an ammonia gas inlet 5 is arranged in the front flow path on the exhaust gas introduction side of the catalyst bed 4, and ammonia gas is introduced into the combustion exhaust gas 6 flowing through the pipe 1. A widely known removal method involves adding and mixing ammonia through the port 5, catalytically reducing nitrogen oxides in the exhaust gas in the catalyst bed 4, and releasing the nitrogen oxides into the atmosphere as harmless nitrogen gas.
しカルながら、このような従来の除去法は、アンモニ
アを最初の触媒床4の前方流路に全量を添加するので、
排ガスの流量および温度の変動によりNH、HSO。However, such conventional removal methods add the entire amount of ammonia to the forward flow path of the first catalyst bed 4.
NH, HSO due to fluctuations in exhaust gas flow rate and temperature.
、(NH。)。SO、、(NH3)、(SO。)y等の
硫酸アンモニウム化合物が一度に多量に生成し、排ガス
導入側の触媒前面の表面に前記硫酸アンモニウム化合物
が付着して、触媒活性を著しく減ずるいわゆる触媒の被
毒現象が生じ、除去効率が著しく低下する致命的な欠点
がある。本発明の排ガス中の窒素酸化物の除去法は、排
ガス中の窒素酸化物をアンモニア添加により触媒床を用
いて接触還元除去する排ガス中の窒素酸化物の除去法に
おいて、排ガス管路中にセラミックハニカム構造体表面
に触媒物質を担持した複数の触媒床をガス流出方向に所
定の間隔をおいて設置し、該各触媒床のガス流入側にそ
れぞれアンモニアガス導入口を配置して、流入排ガスの
減少時にアンモニアガスをガス流出側の触媒床ほど優先
して選択的に供給するよう、アンモニアガス添加個所を
調節制御し、触媒床を選択的に活用する排ガス中の窒素
酸化物の除去法であり、上述した従来の欠点を解決し、
(NH4)x(SO4),等による触媒の被毒現象を軽
減し、触媒の寿命を伸ぱすとともに、除去効率の向上が
得られる窒素酸化物の除去法てある。, (NH.). Ammonium sulfate compounds such as SO, (NH3), (SO. This has the fatal disadvantage of causing a poisonous phenomenon and significantly reducing removal efficiency. The method for removing nitrogen oxides from exhaust gas of the present invention is to remove nitrogen oxides from exhaust gas by catalytic reduction using a catalyst bed by adding ammonia. A plurality of catalyst beds carrying a catalyst material on the surface of the honeycomb structure are installed at predetermined intervals in the gas outflow direction, and an ammonia gas inlet is arranged on the gas inflow side of each catalyst bed, so that the inflow exhaust gas is This is a method for removing nitrogen oxides from exhaust gas that selectively utilizes the catalyst bed by adjusting and controlling the ammonia gas addition point so that ammonia gas is selectively supplied to the catalyst bed on the gas outlet side when the exhaust gas is reduced. , solving the above-mentioned conventional drawbacks,
There is a method for removing nitrogen oxides that reduces the phenomenon of catalyst poisoning caused by (NH4)x(SO4), etc., extends the life of the catalyst, and improves the removal efficiency.
本発明の構成を一具体例を示す第2図に基づいて説明す
れば、燃焼排ガスの管路7の中に、コージェライト、ム
ライト、アルミナ等のセラミック質よりなり、貫通孔の
断面形状が円あるいは三角形、四角形、五角形、六角形
、、八角形等の多角形よりなるセラミックハニカム構造
体の薄壁表面上に、触媒金属酸化物よりなる触媒物質を
担持した複数の触媒床8a,8b,8cを、排ガスの流
出方向に所定の間隔をおいて設置する。そして、該各触
媒床8a,8b,8cの排ガス流入側に、それぞれアン
モニア導入口9a,9b,9cを配設して排ガスの流量
、温度、窒素酸化物の含有量等の変動に応じてアンモニ
アの添加.個所を、アンモニアガス導入口9a,9b,
9cのうちて調節制御して、触媒床8a,8b,8cを
選択的に窒素酸化物の浄化触媒床として使用する窒素酸
化物の除去法である。すなわち、例えば稼動率が低下し
て排ガス量が.゛1B程度に減少したときには、全触媒
床を使用する必要はないので、その時にはアンモニアガ
ス導入口9aおよび9bよりのアンモニア添加を止めて
一部の触媒床8cのみで浄化を行なう。The structure of the present invention will be explained based on FIG. 2 showing a specific example. The combustion exhaust gas pipe 7 is made of ceramic material such as cordierite, mullite, alumina, etc., and the cross-sectional shape of the through hole is circular. Alternatively, a plurality of catalyst beds 8a, 8b, 8c in which a catalyst substance made of a catalyst metal oxide is supported on the thin wall surface of a ceramic honeycomb structure made of polygons such as triangles, squares, pentagons, hexagons, and octagons. are installed at predetermined intervals in the exhaust gas outflow direction. Ammonia inlet ports 9a, 9b, 9c are provided on the exhaust gas inflow side of each of the catalyst beds 8a, 8b, 8c, so that ammonia can be injected according to fluctuations in the exhaust gas flow rate, temperature, nitrogen oxide content, etc. Addition of The locations are ammonia gas inlet ports 9a, 9b,
This is a nitrogen oxide removal method in which catalyst beds 8a, 8b, and 8c are selectively used as nitrogen oxide purification catalyst beds by adjusting and controlling the catalyst beds 9c. In other words, for example, the operating rate decreases and the amount of exhaust gas decreases. When the amount is reduced to about 1B, it is not necessary to use all the catalyst beds, so at that time, the addition of ammonia from the ammonia gas inlets 9a and 9b is stopped and purification is performed using only a part of the catalyst bed 8c.
即ち、アンモニアガスの添加を全触媒床の前面側、換言
くすればガス導入側の最初の触媒床8aの前方の導入口
9aより全量加えると、全触媒床8a,8b及び8C1
特に8aが硫酸アンモニウム化合物で被毒するので、ガ
ス量が少ない場合は最終の触媒床8cの前方の導入口9
cのみよりアンモニアガスを導入し、ガス流出側の触媒
床8cのみを選択的に活用するものである。この場合触
媒床8a,8bはアンモニアガスの添加がないので硫酸
アンモニウムによる被毒の全く生じないものである。ま
たガス量が多く、硫安の生成が多い時にはアンモニアの
添加を3分割して、それぞれ113づつのアンモニアを
導入口9a,9b,9cより添加し、複数の触媒床て分
割して浄化作用を行う等、ノアンモニアの添加口を調節
制御して、触媒床を選択的に活用するものである。なお
、複数の触媒床を設置しているので、排ガス量の変動が
特に大きく管路中での排ガスの温度低下が特に著しい場
合は、触媒床全体に同一の触媒物質を使用せす、燃焼炉
に近い触媒床には高温高活性用触媒を使用し、あと温度
低下に応じて、最適の浄化特性を有する触媒物質を使用
することもできるのである。That is, if the entire amount of ammonia gas is added from the front side of all the catalyst beds, in other words, from the introduction port 9a in front of the first catalyst bed 8a on the gas introduction side, all the catalyst beds 8a, 8b and 8C1
In particular, since 8a is poisoned by ammonium sulfate compounds, if the gas amount is small, the inlet 9 in front of the final catalyst bed 8c
Ammonia gas is introduced only through the catalyst bed 8c, and only the catalyst bed 8c on the gas outlet side is selectively utilized. In this case, since no ammonia gas is added to the catalyst beds 8a and 8b, no poisoning by ammonium sulfate occurs. When the amount of gas is large and a large amount of ammonium sulfate is generated, the addition of ammonia is divided into three parts, and 113 ammonia is added each through the inlet ports 9a, 9b, and 9c, and the purification effect is performed by dividing the ammonia into multiple catalyst beds. etc., the catalyst bed is selectively utilized by adjusting and controlling the noammonia addition port. In addition, since multiple catalyst beds are installed, if the fluctuating amount of exhaust gas is particularly large and the temperature of the exhaust gas in the pipes decreases significantly, use the same catalyst material for the entire catalyst bed. It is also possible to use a high-temperature, high-activity catalyst in the catalyst bed near the temperature, and then use a catalyst material with optimal purification properties as the temperature decreases.
なお、1つの触媒床を1個のハニカム構造体で形成する
ことは困難であるので、複数個の単一のハニカム構造体
を平面的あるいは立体的に組合わせて触媒床を形成して
も勿論よいものてある。Note that it is difficult to form one catalyst bed with one honeycomb structure, so it is of course possible to form a catalyst bed by combining a plurality of single honeycomb structures two-dimensionally or three-dimensionally. There are some good ones.
本発明の排ガス中の窒素酸化物の除去法は、以上のべた
とおり複数の触媒床を排ガス管路中のガス流出方向に所
定の間隔をおいて設置し、各触媒床のガス流入側にそれ
ぞれアンモニアガス導入口を設けて、排ガスの温度、流
量、窒素酸化物の含有量その他の変動に応じて、アンモ
ニア添加個所を変更、調節あるいは制御し、複数の触媒
床を選択的に活用するものてあるので、硫安等の生成に
よる触媒の被毒が所定の触媒床にのみ片寄ることが少な
く、触媒の寿命を大幅に伸ばすとともに除去効率の向上
が得られるものてあり、各種の燃焼排ガス中の窒素酸化
物の除去法として使用てき、公害防止の観点よりも極め
て有用な方法である。As described above, the method for removing nitrogen oxides from exhaust gas according to the present invention is to install a plurality of catalyst beds at predetermined intervals in the gas outflow direction in the exhaust gas pipe, and to install each catalyst bed on the gas inflow side of each catalyst bed. An ammonia gas inlet is provided to selectively utilize multiple catalyst beds by changing, adjusting or controlling the ammonia addition point according to fluctuations in exhaust gas temperature, flow rate, nitrogen oxide content, and other factors. Therefore, the poisoning of the catalyst due to the formation of ammonium sulfate, etc. is less likely to be localized to a specific catalyst bed, which greatly extends the life of the catalyst and improves the removal efficiency. It has been used as a method for removing oxides, and is an extremely useful method from the viewpoint of pollution prevention.
第1図は従来のアンモニアガス添加による排ガス中の窒
素酸化物の除去法の1例を模式的に示す説明図であり、
第2図は本発明の排ガス中の窒素酸化物の除去法の1具
体例を模式的に示す説明図である。
1,7・・・・・・管路、2・・・・・・枠、3・・・
・・・粒状触媒、4,8a,8b,8c・・・・・・触
媒床、5,9a,9b,9c・・・・・・アンモニアガ
ス導入口、6・・・・・・燃焼排ガス。FIG. 1 is an explanatory diagram schematically showing an example of a conventional method for removing nitrogen oxides from exhaust gas by adding ammonia gas.
FIG. 2 is an explanatory diagram schematically showing one specific example of the method for removing nitrogen oxides from exhaust gas according to the present invention. 1,7...Pipeline, 2...Frame, 3...
... Granular catalyst, 4, 8a, 8b, 8c... Catalyst bed, 5, 9a, 9b, 9c... Ammonia gas inlet, 6... Combustion exhaust gas.
Claims (1)
床を用いて接触還元除去する排ガス中の窒素酸化物の除
去法において、排ガス管路中にセラミックハニカム構造
体表面に触媒物質を担持した複数の触媒床をガス流出方
向に所定の間隔をおいて設置し、該各触媒床のガス流入
側にそれぞれアンモニアガス導入口を配置して、流入排
ガスの減少時にアンモニアガスをガス流出側の触媒床ほ
ど優先して選択的に供給するように、アンモニアガス添
加個所を調節制御し、触媒床を選択的に活用することを
特徴とする排ガス中の窒素酸化物の除去法。1. In a method for removing nitrogen oxides from exhaust gas by catalytic reduction using a catalyst bed by adding ammonia, a plurality of catalysts having catalyst substances supported on the surface of a ceramic honeycomb structure are used in the exhaust gas pipe. The beds are installed at predetermined intervals in the gas outflow direction, and an ammonia gas inlet is placed on the gas inflow side of each catalyst bed, so that when the inflow exhaust gas decreases, ammonia gas is given priority to the catalyst bed on the gas outflow side. A method for removing nitrogen oxides from exhaust gas, which comprises adjusting and controlling the point at which ammonia gas is added to selectively supply ammonia gas, thereby selectively utilizing a catalyst bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52012686A JPS6044009B2 (en) | 1977-02-08 | 1977-02-08 | Method for removing nitrogen oxides from exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52012686A JPS6044009B2 (en) | 1977-02-08 | 1977-02-08 | Method for removing nitrogen oxides from exhaust gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5397974A JPS5397974A (en) | 1978-08-26 |
| JPS6044009B2 true JPS6044009B2 (en) | 1985-10-01 |
Family
ID=11812250
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52012686A Expired JPS6044009B2 (en) | 1977-02-08 | 1977-02-08 | Method for removing nitrogen oxides from exhaust gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6044009B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4523046A (en) * | 1982-02-25 | 1985-06-11 | Mobil Oil Corporation | Method for gasoline yield enhancement in the fixed bed methanol-to-gasoline process |
-
1977
- 1977-02-08 JP JP52012686A patent/JPS6044009B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5397974A (en) | 1978-08-26 |
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