JPH0924246A - Ammonia injection device in denitration device - Google Patents
Ammonia injection device in denitration deviceInfo
- Publication number
- JPH0924246A JPH0924246A JP7177426A JP17742695A JPH0924246A JP H0924246 A JPH0924246 A JP H0924246A JP 7177426 A JP7177426 A JP 7177426A JP 17742695 A JP17742695 A JP 17742695A JP H0924246 A JPH0924246 A JP H0924246A
- Authority
- JP
- Japan
- Prior art keywords
- ammonia injection
- exhaust gas
- ammonia
- denitration
- gas flow
- 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.)
- Pending
Links
Landscapes
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Nozzles (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明はアンモニアを還元剤
として用いる脱硝装置におけるアンモニア注入装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ammonia injection device in a denitration device that uses ammonia as a reducing agent.
【0002】[0002]
【発明が解決しようとする課題】アンモニアを還元剤と
して用いる脱硝装置において、高効率での脱硝作用を得
るには、アンモニアを排ガス中に均一に分布するよう注
入する必要がある。In a denitration apparatus using ammonia as a reducing agent, it is necessary to inject ammonia so that it is evenly distributed in the exhaust gas in order to obtain a highly efficient denitration action.
【0003】かかるアンモニアの排ガス流路内への均一
な分布を得るには脱硝触媒反応器(以下反応器と略称す
る)の上流のダクトにアンモニアと排ガスを混合するた
めの混合器を設けるとともに、同混合器の直上流にアン
モニア注入ノズル及びこれが装着されるアンモニア注入
母管を設けている。In order to obtain such a uniform distribution of ammonia in the exhaust gas passage, a mixer for mixing ammonia and exhaust gas is provided in the duct upstream of the denitration catalytic reactor (hereinafter abbreviated as a reactor). Immediately upstream of the mixer, an ammonia injection nozzle and an ammonia injection mother tube to which the ammonia injection nozzle is attached are provided.
【0004】上記アンモニア注入ノズル及び母管、並び
に混合器を設ける場合、通常脱硝触媒装置を設置する発
電プラントではこれらの設置スペースに制限があるた
め、図7に示されるように、煙道1の下流端部と反応器
2との間には鉛直方向に段差ができ、これに沿うように
アンモニア注入母管4及び注入ノズルを設けることとな
る。When the above-mentioned ammonia injection nozzle, mother tube, and mixer are installed, the installation space for these is usually limited in a power plant where a denitration catalyst device is installed. Therefore, as shown in FIG. A step is formed in the vertical direction between the downstream end and the reactor 2, and the ammonia injection mother tube 4 and the injection nozzle are provided along the step.
【0005】即ち、図7において、煙道1の下流端部と
反応器2とは鉛直方向に段差を存して取付けられてい
る。また、3は入口ダクト、4は多数のアンモニア注入
ノズル(図示省略)が取付けられたアンモニア注入母
管、9は同注入ノズルから注入されたアンモニアと排ガ
スとを混合するための混合器である。That is, in FIG. 7, the downstream end of the flue 1 and the reactor 2 are attached with a step in the vertical direction. Further, 3 is an inlet duct, 4 is an ammonia injection mother tube to which a large number of ammonia injection nozzles (not shown) are attached, and 9 is a mixer for mixing the ammonia injected from the injection nozzle and the exhaust gas.
【0006】上記アンモニア注入ノズルは、上記反応器
2の高さ方向に列設されたアンモニア注入母管4の軸線
に直角方向に夫々取付けられ、開口部が排ガス流の下流
側(反応器2側)へ指向されている。The ammonia injection nozzles are respectively attached at right angles to the axis of the ammonia injection mother pipes 4 arranged in the height direction of the reactor 2, and the openings are located on the downstream side of the exhaust gas flow (reactor 2 side). ).
【0007】このため、上記従来のものにあっては、図
7のように煙道1の終端部と反応器2との間に鉛直方向
の段差がある場合には、アンモニア注入ノズルから噴出
されるアンモニアの分布が反応器2の上部側で少なく、
中央部及び下部寄りの部位で多くなるというように、反
応器2の入口部においてアンモニアの分布が不均一とな
り、脱硝効率が低下するという問題点を抱えている。Therefore, in the above-mentioned conventional apparatus, when there is a vertical step between the end portion of the flue 1 and the reactor 2 as shown in FIG. Distribution of ammonia is small on the upper side of the reactor 2,
There is a problem in that the distribution of ammonia becomes non-uniform at the inlet of the reactor 2 and the denitrification efficiency decreases, as the amount increases in the central portion and the portion near the lower portion.
【0008】本発明の目的は、排ガス路の脱硝触媒反応
器の上流にアンモニア注入ノズルを設けた脱硝装置にお
いて、上記反応器へ導入されるアンモニアの分布を排ガ
ス流路断面において均一化して、脱硝効率が向上せしめ
られた脱硝装置を提供することである。An object of the present invention is to provide a denitration device having an ammonia injection nozzle upstream of a denitration catalytic reactor in an exhaust gas passage, in which the distribution of ammonia introduced into the reactor is made uniform in the cross section of the exhaust gas passage to remove denitration. It is an object of the present invention to provide a denitration device having improved efficiency.
【0009】[0009]
【課題を解決するための手段】本発明は、脱硝触媒反応
器の入口へ向けてアンモニアを噴出するためのアンモニ
ア注入母管及び同母管に取付けられたアンモニア注入ノ
ズルの向き及び角度を、排ガスダクトの排ガス流路形状
に沿って変化せしめ、アンモニア注入ノズルから噴出さ
れるアンモニアを排ガス中に均一に分布せしめられるよ
うにしたことを要旨としており、その具体的構成は、窒
素酸化物を含む排ガスが流過する排ガス路の脱硝触媒反
応器の上流に、アンモニア注入母管を排ガス流に略直角
方向に多数設置し、同注入母管に取付けられたアンモニ
ア注入ノズルよりアンモニアを注入して脱硝触媒により
接触還元を行う排ガスの脱硝装置において、上記アンモ
ニア注入母管及びアンモニア注入ノズルは、同注入ノズ
ルと上記脱硝触媒反応器との間のダクトの流路形状に沿
って各ノズルの噴出口の向き及び角度が変化せしめられ
て配設されたことである。According to the present invention, the direction and angle of an ammonia injection mother pipe for ejecting ammonia toward the inlet of a denitration catalytic reactor and an ammonia injection nozzle attached to the mother mother pipe are defined as follows. The gist is that it is changed along the exhaust gas flow path shape of the duct so that the ammonia ejected from the ammonia injection nozzle can be evenly distributed in the exhaust gas. A large number of ammonia injection mother tubes are installed in the exhaust gas flow upstream of the denitration catalyst reactor in a direction substantially perpendicular to the exhaust gas flow, and ammonia is injected from the ammonia injection nozzle attached to the same injection mother tube to remove the denitration catalyst. In an exhaust gas denitration apparatus that performs catalytic reduction by means of an exhaust gas, the ammonia injection mother pipe and the ammonia injection nozzle are Orientation and angle of the jetting ports of the nozzles along the flow path shape of the duct between the 応器 is that is disposed contain altered.
【0010】これにより、複数のアンモニア注入母管及
び注入ノズルは、ダクトの流路の形状が、例えば下流側
へ拡開されるように変化しても、同母管及びノズルの個
々の向き及び取付角度が流路の形状に応じて変化せしめ
られて装備されることから、注入ノズルから反応器側へ
向かって噴出されるアンモニアは反応器入口の排ガス流
路断面に均一に分布することとなる。As a result, the plurality of ammonia injection mother tubes and the plurality of nozzles have different directions of the mother tubes and nozzles even if the shape of the duct flow passage is changed so as to be expanded downstream. Since the mounting angle is changed according to the shape of the flow path and the equipment is equipped, the ammonia ejected from the injection nozzle toward the reactor side is uniformly distributed in the exhaust gas flow path cross section at the reactor inlet. .
【0011】従って脱硝触媒反応器にはアンモニアが排
ガス中に均一に分布されて導入されることとなり、脱硝
効率が向上する。Therefore, ammonia is uniformly distributed in the exhaust gas and introduced into the denitration catalytic reactor, and the denitration efficiency is improved.
【0012】また好ましくは、上記アンモニア注入ノズ
ルを、上記アンモニア注入母管1本に対して2個取付
け、その噴出口中心の取付角を上記ダクトの流路形状に
合わせて変化せしるように構成する。Preferably, two ammonia injection nozzles are attached to one ammonia injection mother pipe, and the attachment angle at the center of the ejection port is changed according to the flow path shape of the duct. Configure.
【0013】これにより、アンモニア注入ノズルの母管
への取付状態を排ガスの流路形状に応じて変化させるこ
とができ、アンモニアの均一な分布を得るためのさらな
る微調整が可能となる。As a result, the mounting state of the ammonia injection nozzle on the mother pipe can be changed according to the shape of the flow path of the exhaust gas, and further fine adjustment for obtaining a uniform distribution of ammonia becomes possible.
【0014】また、上記ダクト内のアンモニア注入母管
の上流側に排ガス流を案内するための整流部材を排ガス
流路に略直角な方向に複数枚並設することも本発明の要
旨とする一形態である。Another feature of the present invention is to install a plurality of rectifying members for guiding the exhaust gas flow upstream of the ammonia injection mother pipe in the duct in a direction substantially perpendicular to the exhaust gas passage. It is a form.
【0015】このように構成すれば、アンモニア注入母
管及び注入ノズル上流側の排ガスが整流部材によって流
路断面全体を均一に流れるように整流されて、上記母管
及びノズルへと導かれる。これにより、上記に加えて排
ガスとアンモニアとの混合がさらに均一に行われる。According to this structure, the exhaust gas on the upstream side of the ammonia injection mother pipe and the injection nozzle is rectified by the rectifying member so as to flow uniformly over the entire cross section of the flow passage, and is guided to the mother pipe and the nozzle. As a result, in addition to the above, the exhaust gas and the ammonia are mixed more uniformly.
【0016】[0016]
【発明の実施の形態】以下図面を参照して本発明の実施
形態について詳細に説明する。図1,2には本発明の実
施の第1形態に係るボイラ排ガス路に設置された脱硝装
置のアンモニア注入装置の構成図が示されている。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below with reference to the drawings. 1 and 2 are configuration diagrams of an ammonia injection device of a denitration device installed in a boiler exhaust gas passage according to a first embodiment of the present invention.
【0017】図1,2は、ボイラ(図示せず)からの排
ガスが流過する煙道1の終端部に対して反応器2が水平
方向に拡がりかつずれて配置された脱硝装置であり、図
において3は煙道1と脱硝触媒反応器(以下反応器と略
称する)2との間を接続する入口ダクトであり、同入口
ダクト3は上記煙道1と反応器2との上記のような配置
に伴い、水平方向において一方側が反応器2へ向けて拡
開された形状となっている。FIGS. 1 and 2 show a denitration device in which a reactor 2 is horizontally extended and displaced with respect to a terminal portion of a flue 1 through which exhaust gas from a boiler (not shown) flows, In the figure, 3 is an inlet duct connecting between the flue 1 and a denitration catalytic reactor (hereinafter abbreviated as a reactor) 2, and the inlet duct 3 is the same as the flue 1 and the reactor 2 described above. With this arrangement, one side is expanded toward the reactor 2 in the horizontal direction.
【0018】5はアンモニア注入母管であり上記入口ダ
クト3の下流部の拡開部に、その軸線5aを鉛直方向に
置き、排ガスの流路断面に均一間隔で多数列設されてい
る。Reference numeral 5 denotes an ammonia injection mother pipe, which has an axial line 5a arranged vertically in the expanded portion at the downstream portion of the inlet duct 3 and is arranged in a large number in a row in the exhaust gas flow passage cross section.
【0019】上記各アンモニア注入母管5には、図2に
示されるように、2本のアンモニア注入ノズル6が排ガ
ス流の下流側へ向けて取付けられている。上記各アンモ
ニア注入母管5は、アンモニア注入ノズル6,6の向き
をこれより噴出されるアンモニアが反応器2入口の混合
部9において均一に分布するようにするため、これのア
ンモニア注入ノズル6,6取付中心線Yとボイラ中心線
Zに平行な軸線Z1 とのなす角度θを、入口ダクト3の
水平方向における拡がり度合に応じて変化せしめてい
る。As shown in FIG. 2, two ammonia injection nozzles 6 are attached to each of the ammonia injection mother pipes 5 toward the downstream side of the exhaust gas flow. The ammonia injection mother pipes 5 are arranged so that the ammonia injected from the ammonia injection nozzles 6 and 6 can be uniformly distributed in the mixing portion 9 at the inlet of the reactor 2 so that the ammonia injected therefrom can be uniformly distributed. 6. The angle θ formed by the mounting center line Y and the axis Z 1 parallel to the boiler center line Z is changed according to the degree of expansion of the inlet duct 3 in the horizontal direction.
【0020】そして各アンモニア注入母管5に取付けら
れる2個のアンモニア注入ノズル6,6は一定の取付角
βを存して取付けられている。The two ammonia injection nozzles 6 and 6 attached to each ammonia injection mother pipe 5 are attached with a constant attachment angle β.
【0021】図1,2に示される脱硝装置のアンモニア
注入装置における上記アンモニア注入母管5及びアンモ
ニア注入ノズル6,6の配置態様の1例を示すと、アン
モニア注入ノズル6,6の取付角β=30°とし、入口
ダクト3内の排ガス流路がボイラ中心Zと略平行な部位
(図1のボイラ中心Z寄りの部位)においてはθ=10
°、最も拡開された部位(図1のN部近傍)においては
θ=45°、その中間部はθ=10°〜45°(中心は
θ=30°程度)の範囲で変化せしめている。An example of the arrangement of the ammonia injection mother pipe 5 and the ammonia injection nozzles 6 and 6 in the ammonia injection device of the denitration apparatus shown in FIGS. = 30 °, and θ = 10 at a portion where the exhaust gas flow passage in the inlet duct 3 is substantially parallel to the boiler center Z (a portion near the boiler center Z in FIG. 1).
, Θ = 45 ° in the most widened part (near the N part in FIG. 1), and the middle part is changed in the range of θ = 10 ° to 45 ° (center is about θ = 30 °). .
【0022】4は入口ダクト3内に排ガス流の流路断面
に沿って複数枚設けられた整流板であり、同整流板4は
上記入口ダクト3の流路形状に応じて適宜屈曲され、煙
道1の終端部とアンモニア注入母管5との間の排ガス流
路が滑らかに拡開されるようにしている。Reference numeral 4 denotes a straightening plate provided in the inlet duct 3 along the cross section of the flow path of the exhaust gas flow. The straightening plate 4 is appropriately bent according to the shape of the flow path of the inlet duct 3 to produce smoke. The exhaust gas flow passage between the end of the passage 1 and the ammonia injection mother pipe 5 is smoothly expanded.
【0023】尚、図2において、51はアンモニア注入
母管5支持用のブラケット、52はアッシュエロージョ
ン防止用のプロテクタ板である。In FIG. 2, reference numeral 51 is a bracket for supporting the ammonia injection mother pipe 5, and 52 is a protector plate for preventing ash erosion.
【0024】上記のように構成されたアンモニア注入装
置を備えた脱硝装置の運転時において、ボイラからの排
ガスは煙道1から入口ダクト3に導入され、ここで整流
板4によってガイドされて水平方向に均一に拡がり、ア
ンモニア注入母管5側へと流れる。During the operation of the denitration apparatus equipped with the ammonia injecting device constructed as described above, the exhaust gas from the boiler is introduced from the flue 1 into the inlet duct 3, where it is guided by the straightening vanes 4 and horizontally. Uniformly spreads and flows toward the ammonia injection mother pipe 5 side.
【0025】そしてこの排ガス中に、排ガス流路断面に
沿って上記のように角度及び向きを変えて多数列設され
たアンモニア注入母管5の夫々に取付けられたアンモニ
ア注入ノズル6,6からアンモニアを噴出せしめる。Then, in the exhaust gas, ammonia is injected from the ammonia injection nozzles 6 and 6 attached to each of the ammonia injection mother pipes 5 which are arranged in multiple rows at different angles and directions as described above along the exhaust gas passage section. Squirt out.
【0026】この際において、アンモニア注入母管5及
びアンモニア注入ノズル6,6は入口ダクト3内の排ガ
ス流路の拡がり度合に応じてその向き及び角度が変化せ
しめられているので、各注入ノズル6,6から噴出され
るアンモニアは反応器2の入口部(混合部9)において
均一に分布し、排ガスと混合されて反応器2内にむらな
く導入される。At this time, the directions and angles of the ammonia injection mother pipe 5 and the ammonia injection nozzles 6 and 6 are changed according to the extent of expansion of the exhaust gas flow passage in the inlet duct 3, so that each injection nozzle 6 , 6 are evenly distributed at the inlet (mixing part 9) of the reactor 2, mixed with the exhaust gas, and uniformly introduced into the reactor 2.
【0027】図3,4には本発明の実施の第2形態が示
されている。この実施形態においては、上記煙道1の終
端部に対して反応器2が鉛直方向に拡がり、かつ上方に
ずれて配置されており、入口ダクト3は煙道1の終端部
から下部が略水平に、上部側になるに従い反応器2側へ
向けて拡開された形状となっている。A second embodiment of the present invention is shown in FIGS. In this embodiment, the reactor 2 is arranged to extend vertically with respect to the end of the flue 1 and is displaced upward, and the inlet duct 3 is substantially horizontal from the end of the flue 1 to the bottom. In addition, the shape is such that it expands toward the reactor 2 side toward the upper side.
【0028】そして、アンモニア注入母管5は、その軸
線5aを水平方向に置き、排ガスの流路断面に均一間隔
で多数配設されるとともに、各母管5には、図4に示さ
れるように、2個のアンモニア注入ノズル6,6がその
噴出口を下流の反応器2側へ向けて、一定の取付角αに
て取付けられている。The ammonia injection mother pipes 5 are arranged with their axis 5a in the horizontal direction and are arranged in a large number at even intervals in the cross section of the flow path of the exhaust gas. In each mother pipe 5, as shown in FIG. In addition, the two ammonia injection nozzles 6 and 6 are attached at a fixed attachment angle α with their ejection ports facing the downstream reactor 2 side.
【0029】上記アンモニア注入母管5は、この実施形
態の場合は、アンモニア注入ノズル6から噴出されるア
ンモニアの特に鉛直方向における分布の不均一が発生し
ないようにするため、水平線Wに対する注入ノズル6,
6の取付中心線Yのなす角度θを鉛直方向における入口
ダクト3の拡がり度合に応じて変化せしめている。In the case of this embodiment, the above-mentioned ammonia injection mother pipe 5 does not cause non-uniform distribution of the ammonia ejected from the ammonia injection nozzle 6, especially in the vertical direction, so that the injection nozzle 6 with respect to the horizontal line W will not be generated. ,
The angle θ formed by the mounting center line Y of 6 is changed according to the degree of expansion of the inlet duct 3 in the vertical direction.
【0030】即ち、入口ダクト3内の排ガス流れが略水
平な下部ではθを小さく反応器2側へ向けて拡開された
上部ではθを大きく設定しており、図3,4に示される
実施形態での好適な一例を示すと、排ガス流れが略水平
な下部においてはθ=5°、最も拡開された上部におい
てはθ=20°、その中間部はθ=5°〜20°の範囲
で変化せしめている。That is, θ is set small in the lower portion where the exhaust gas flow in the inlet duct 3 is substantially horizontal and set large in the upper portion expanded toward the reactor 2 side. As a preferable example of the form, θ = 5 ° in the lower part where the exhaust gas flow is substantially horizontal, θ = 20 ° in the most expanded upper part, and θ = 5 ° to 20 ° in the middle part. Is changing.
【0031】またアンモニア注入ノズル6,6の母管5
への取付角αは排ガス流が略水平な下部及び中間部で大
きく(例えばα=45°程度)、排ガス流が拡開される
上部で小さく(例えばα=30°程度)設定して、上記
母管5の鉛直方向傾き角θと調和せしめ、注入ノズル
6,6から噴出されるアンモニアの特に鉛直方向におけ
る不均一分布の形成を防止し、全体として均一な分布を
形成せしめている。The mother pipe 5 of the ammonia injection nozzles 6 and 6
The attachment angle α to the exhaust gas flow is set to be large in the lower part and the middle part where the exhaust gas flow is substantially horizontal (for example, α = 45 °) and small in the upper part where the exhaust gas flow is expanded (for example, α = 30 °). The vertical inclination angle θ of the mother tube 5 is harmonized to prevent the formation of a non-uniform distribution of the ammonia ejected from the injection nozzles 6 and 6, particularly in the vertical direction, thereby forming a uniform distribution as a whole.
【0032】図5,6には本発明の実施の第3形態が示
されている。この実施形態においては、アンモニア注入
母管5及びアンモニア注入ノズル6の下流側、つまり反
応器2の入口部にアンモニアと排ガスとを混合せしめる
混合器9を設置しており、かかる構成以外は図1,2の
実施形態と同一である。5 and 6 show a third embodiment of the present invention. In this embodiment, a mixer 9 for mixing ammonia and exhaust gas is installed on the downstream side of the ammonia injection mother pipe 5 and the ammonia injection nozzle 6, that is, at the inlet of the reactor 2. , 2 of the embodiment.
【0033】即ち、この実施形態においては、図1,2
に示される実施形態と同様、煙道1の終端部に対し、反
応器2が水辺方向に未広に拡がりかつずれて配置され、
アンモニア注入母管5はその軸線5aを鉛直方向に於い
て排ガスの流路断面に沿って均一な間隔で多数配設され
ている。That is, in this embodiment, FIGS.
In the same manner as the embodiment shown in FIG. 2, the reactor 2 is arranged so as not to spread in the waterside direction and displaced from the terminal end of the flue 1,
A large number of the ammonia injection mother tubes 5 are arranged in the vertical direction along the exhaust gas passage section at a uniform interval in the vertical direction.
【0034】そしてこの実施形態においては、アンモニ
ア注入母管5の傾斜角θとともに2個のアンモニア注入
ノズル6,6の取付角βも入口ダクト3の流路形状に応
じて変化せしめており、アンモニア注入母管5の傾斜角
θが排ガス流れのボイラ中心線Zに平行な部位ではθ=
0°、入口ダクトの拡開部ではθ=30°、その中間部
でθ=20°程度が好適である。In this embodiment, the inclination angle θ of the ammonia injection mother pipe 5 and the mounting angle β of the two ammonia injection nozzles 6 and 6 are also changed according to the shape of the flow path of the inlet duct 3. At a portion where the inclination angle θ of the injection mother pipe 5 is parallel to the boiler center line Z of the exhaust gas flow, θ =
It is preferable that 0 °, θ = 30 ° in the expanded portion of the inlet duct, and θ = 20 ° in the intermediate portion.
【0035】またアンモニア注入ノズル6,6の取付角
βはボイラ中心線寄り部位及び流路の中間部位ではβ=
30°、入口ダクト3が拡開された部位ではβ=45°
程度、その中間はβ=30°〜45°の範囲で滑らかに
変化せしめるのが好適である。Further, the mounting angle β of the ammonia injection nozzles 6, 6 is β = at the portion near the center line of the boiler and the intermediate portion of the flow path.
30 °, β = 45 ° at the site where the inlet duct 3 is expanded
It is preferable to smoothly change the degree and the middle thereof in the range of β = 30 ° to 45 °.
【0036】[0036]
【発明の効果】本発明は以上のように構成されており、
請求項1ないし2の発明によれば、アンモニア注入母管
及びアンモニア注入ノズルの向き及び角度を、反応器上
流側の排ガスダクトの流路形状に沿って変化せしめて設
けたので、アンモニア注入装置が装備される排ガスダク
トの形状が拡大あるいは縮小しても、アンモニアはこの
流路変化に応じて噴出されることとなり、反応器にアン
モニアが排ガス中に均一に分布した状態で供給され、反
応の脱硝効率が向上する。The present invention is configured as described above.
According to the invention of claims 1 and 2, since the direction and the angle of the ammonia injection mother pipe and the ammonia injection nozzle are changed along the flow path shape of the exhaust gas duct on the upstream side of the reactor, the ammonia injection device is provided. Even if the shape of the equipped exhaust gas duct expands or contracts, ammonia will be ejected according to this flow path change, and ammonia will be supplied to the reactor in a state where it is evenly distributed in the exhaust gas, and the denitration of the reaction will occur. Efficiency is improved.
【0037】また、アンモニアを均一に分布せしめるた
めに格別な流路長さを要さず、従って脱硝システム全体
の長さが短縮される。Further, since the ammonia is uniformly distributed, no special flow path length is required, so that the total length of the denitration system is shortened.
【0038】また請求項3の発明によれば、整流部材に
よってアンモニア注入母管5及びノズル6に流入する排
ガス流の分布が均一となり、アンモニアと排ガスとが万
遍なく混合せしめられる。According to the third aspect of the invention, the distribution of the exhaust gas flow flowing into the ammonia injection mother pipe 5 and the nozzle 6 is made uniform by the rectifying member, so that the ammonia and the exhaust gas are evenly mixed.
【図1】本発明の実施の第1形態に係るボイラ排ガス用
脱硝装置のアンモニア注入装置の構成図。FIG. 1 is a configuration diagram of an ammonia injection device of a boiler exhaust gas denitration device according to a first embodiment of the present invention.
【図2】図1におけるアンモニア注入母管及び注入ノズ
ルの拡大構造図。FIG. 2 is an enlarged structural diagram of an ammonia injection mother tube and an injection nozzle in FIG.
【図3】本発明の実施の第2形態に係る図1応当図。FIG. 3 is an illustration corresponding to FIG. 1 according to a second embodiment of the present invention.
【図4】本発明の実施の第2形態に係る図2応当図。FIG. 4 is an illustration corresponding to FIG. 2 according to a second embodiment of the present invention.
【図5】本発明の実施の第3形態に係る図1応当図。FIG. 5 is a view corresponding to FIG. 1 according to a third embodiment of the present invention.
【図6】本発明の実施の第3形態に係る図2応当図。FIG. 6 is an illustration corresponding to FIG. 2 according to the third embodiment of the present invention.
【図7】従来の脱硝装置を示す図1応当図。FIG. 7 is a corresponding view of FIG. 1 showing a conventional denitration device.
1 煙道 2 脱硝触媒反応器 3 入口ダクト 4 整流板 5 アンモニア注入母管 6 アンモニア注入ノズル 9 混合器 1 Flue 2 DeNOx catalyst reactor 3 Inlet duct 4 Rectifier plate 5 Ammonia injection mother tube 6 Ammonia injection nozzle 9 Mixer
Claims (3)
ス路の脱硝触媒反応器の上流に、アンモニア注入母管を
排ガス流に略直角方向に多数設置し、同注入母管に取付
けられたアンモニア注入ノズルよりアンモニアを注入し
て脱硝触媒により接触還元を行う排ガスの脱硝装置にお
いて、上記アンモニア注入母管及びアンモニア注入ノズ
ルは、同注入ノズルと上記脱硝触媒反応器との間のダク
トの流路形状に沿って各ノズルの噴出口の向き及び角度
が変化せしめられて配設されたことを特徴とする脱硝装
置のアンモニア注入装置。1. A large number of ammonia injection mother tubes are installed in the exhaust gas flow upstream of the denitration catalytic reactor through which the exhaust gas containing nitrogen oxides flows, and are attached to the same. In an exhaust gas denitration apparatus that injects ammonia from an ammonia injection nozzle to perform catalytic reduction with a denitration catalyst, the ammonia injection mother pipe and the ammonia injection nozzle are duct flow paths between the injection nozzle and the denitration catalyst reactor. An ammonia injection device for a denitration device, characterized in that the direction and the angle of the ejection port of each nozzle are changed according to the shape.
モニア注入母管1本に対して2個取付けられ、その噴出
口中心の取付角を上記ダクトの流路形状に合わせて変化
せしめてなる請求項1記載の脱硝装置のアンモニア注入
装置。2. The two ammonia injection nozzles are attached to one ammonia injection mother pipe, and the attachment angle at the center of the ejection port is changed according to the flow path shape of the duct. Ammonia injection device of the denitration device described.
流側に排ガス流を案内するための整流部材を排ガス流路
に略直角な方向に複数枚並設してなる請求項1記載の脱
硝装置のアンモニア注入装置。3. The denitration device according to claim 1, wherein a plurality of rectifying members for guiding the exhaust gas flow are arranged in parallel in a direction substantially perpendicular to the exhaust gas flow path on the upstream side of the ammonia injection mother pipe in the duct. Ammonia injector.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7177426A JPH0924246A (en) | 1995-07-13 | 1995-07-13 | Ammonia injection device in denitration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7177426A JPH0924246A (en) | 1995-07-13 | 1995-07-13 | Ammonia injection device in denitration device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0924246A true JPH0924246A (en) | 1997-01-28 |
Family
ID=16030733
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7177426A Pending JPH0924246A (en) | 1995-07-13 | 1995-07-13 | Ammonia injection device in denitration device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0924246A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003293734A (en) * | 2002-03-29 | 2003-10-15 | Mitsubishi Fuso Truck & Bus Corp | NOx CLEANING DEVICE FOR INTERNAL COMBUSTION ENGINE |
WO2008142893A1 (en) * | 2007-05-18 | 2008-11-27 | Bosch Corporation | Exhaust emission purifier |
JP2014061514A (en) * | 2013-09-11 | 2014-04-10 | Mitsubishi Heavy Ind Ltd | Exhaust gas treatment device and exhaust gas treatment system |
CN107051200A (en) * | 2016-12-28 | 2017-08-18 | 华电电力科学研究院 | A kind of rotary ammonia-spraying grid applied to SCR denitration system |
JP2017150790A (en) * | 2016-02-26 | 2017-08-31 | 三菱日立パワーシステムズ株式会社 | Exhaust duct and boiler, and method of removing solid particulate |
WO2019054108A1 (en) | 2017-09-15 | 2019-03-21 | 三菱日立パワーシステムズ株式会社 | Dinitrifcation apparatus for coal fired boiler |
KR20200096098A (en) | 2019-02-01 | 2020-08-11 | 미츠비시 히타치 파워 시스템즈 가부시키가이샤 | Reductant supply device and method for operating reductant supply device |
CN112870958A (en) * | 2021-03-19 | 2021-06-01 | 中国华电科工集团有限公司 | Ammonia spraying device and flue gas denitration device |
WO2021161695A1 (en) * | 2020-02-13 | 2021-08-19 | 三菱パワー株式会社 | Denitration device and boiler |
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JPS58153522A (en) * | 1982-03-08 | 1983-09-12 | Hitachi Ltd | Stack gas denitration apparatus |
JPS61293526A (en) * | 1985-06-24 | 1986-12-24 | Mitsubishi Heavy Ind Ltd | Ammonia injection apparatus |
JPS63283726A (en) * | 1987-05-13 | 1988-11-21 | Mitsubishi Heavy Ind Ltd | Gas denitration device by ammonia reduction |
JPS63310626A (en) * | 1987-06-09 | 1988-12-19 | Tokyo Electric Power Co Inc:The | Heat exchanger for steam power plant |
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JPS58153522A (en) * | 1982-03-08 | 1983-09-12 | Hitachi Ltd | Stack gas denitration apparatus |
JPS61293526A (en) * | 1985-06-24 | 1986-12-24 | Mitsubishi Heavy Ind Ltd | Ammonia injection apparatus |
JPS63283726A (en) * | 1987-05-13 | 1988-11-21 | Mitsubishi Heavy Ind Ltd | Gas denitration device by ammonia reduction |
JPS63310626A (en) * | 1987-06-09 | 1988-12-19 | Tokyo Electric Power Co Inc:The | Heat exchanger for steam power plant |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003293734A (en) * | 2002-03-29 | 2003-10-15 | Mitsubishi Fuso Truck & Bus Corp | NOx CLEANING DEVICE FOR INTERNAL COMBUSTION ENGINE |
WO2008142893A1 (en) * | 2007-05-18 | 2008-11-27 | Bosch Corporation | Exhaust emission purifier |
JP2008286134A (en) * | 2007-05-18 | 2008-11-27 | Bosch Corp | Exhaust emission control device |
US8375703B2 (en) | 2007-05-18 | 2013-02-19 | Ud Trucks Corporation | Exhaust gas purification device |
JP2014061514A (en) * | 2013-09-11 | 2014-04-10 | Mitsubishi Heavy Ind Ltd | Exhaust gas treatment device and exhaust gas treatment system |
JP2017150790A (en) * | 2016-02-26 | 2017-08-31 | 三菱日立パワーシステムズ株式会社 | Exhaust duct and boiler, and method of removing solid particulate |
CN107051200A (en) * | 2016-12-28 | 2017-08-18 | 华电电力科学研究院 | A kind of rotary ammonia-spraying grid applied to SCR denitration system |
WO2019054108A1 (en) | 2017-09-15 | 2019-03-21 | 三菱日立パワーシステムズ株式会社 | Dinitrifcation apparatus for coal fired boiler |
KR20200096098A (en) | 2019-02-01 | 2020-08-11 | 미츠비시 히타치 파워 시스템즈 가부시키가이샤 | Reductant supply device and method for operating reductant supply device |
WO2021161695A1 (en) * | 2020-02-13 | 2021-08-19 | 三菱パワー株式会社 | Denitration device and boiler |
JP2021126619A (en) * | 2020-02-13 | 2021-09-02 | 三菱パワー株式会社 | Denitration device and boiler |
TWI778501B (en) * | 2020-02-13 | 2022-09-21 | 日商三菱動力股份有限公司 | Denitrification device and boiler |
CN112870958A (en) * | 2021-03-19 | 2021-06-01 | 中国华电科工集团有限公司 | Ammonia spraying device and flue gas denitration device |
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