JPH025445B2 - - Google Patents

Info

Publication number
JPH025445B2
JPH025445B2 JP54152510A JP15251079A JPH025445B2 JP H025445 B2 JPH025445 B2 JP H025445B2 JP 54152510 A JP54152510 A JP 54152510A JP 15251079 A JP15251079 A JP 15251079A JP H025445 B2 JPH025445 B2 JP H025445B2
Authority
JP
Japan
Prior art keywords
duct
denitrification
catalyst layer
reactor
exhaust 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.)
Expired - Lifetime
Application number
JP54152510A
Other languages
Japanese (ja)
Other versions
JPS5676226A (en
Inventor
Hiroshi Masutomi
Keizo Nagaoka
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP15251079A priority Critical patent/JPS5676226A/en
Publication of JPS5676226A publication Critical patent/JPS5676226A/en
Publication of JPH025445B2 publication Critical patent/JPH025445B2/ja
Granted legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

【発明の詳細な説明】 <産業上の利用分野> この発明は熱変形とこれに伴なうクラツクによ
るガス漏れなどの虞れのない排ガスを脱硝する装
置の構造に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to the structure of an apparatus for denitrifying exhaust gas without the risk of gas leakage due to thermal deformation and accompanying cracks.

<従来の技術及びその問題点> 乾式排ガス脱硝装置は、高温のボイラ排ガス流
路中に触媒層を形成し、上流において、アンモニ
ア等の脱硝剤を注入することにより、触媒層通過
時に排ガス中の窒素酸化物を水(H2O)と窒素
ガス(N2)に分解するものである。このうちパ
ラレルフロー式脱硝反応器は板状触媒、ハニカム
触媒等によつて形成した触媒層を内蔵する装置で
あつて、ガスが触媒層を通過する際の圧力損失が
少ないという特徴がある。このため、パラレルフ
ロー式脱硝反応器は、既設のボイラにあつては、
新規に送風機等を設けることなく節炭器出口と空
気予熱器の間に配置して使用できるという利点が
ある。しかし節炭器および空気予熱器はいづれも
ボイラのダクト内に配置してあるため、脱硝反応
器に流入されるべき排ガスはいづれかの位置にお
いて流れ方向を180゜反転させねばならない。通常
排ガスの流れ方向の反転は脱硝反応器において行
なわれているもので、第1図にこの排ガス流れ方
向を反転させる形式の従来型脱硝反応器の一例の
構造を示す。排ガスは入口ダクト12を通過して
脱硝反応触媒層6に至り、この脱硝反応触媒層6
を通過した後整流板8により流れ方向を転換して
出口ダクト7に至る。この脱硝反応器において出
口ダクト7は脱硝反応触媒層6を支持する補強鉄
骨11により支持されている。すなわち、補強鉄
骨11は下部ダクト12の天井部12aを挿通し
て前記上記ダクト7の底板7aを支持することに
より上部ダクト7を支持している。しかし上部ダ
クト7と下部ダクト12の間には空間部14aが
形成されるため各ダクト内部とこの空間部14と
の間に大きな温度差を生じ、脱硝反応器全体が熱
変形する虞れがある。このため第1図で横方向の
変位を吸収するための伸縮部材10a,10ob
を、また上下方向の変位の吸収のため下部ダクト
12と上部ダクト7の接続部にも別個に伸縮部材
15を配置せねばならず、全体として装置の構造
が複雑化する。さらに補強鉄骨11も下部ダクト
12内と、空間部14に位置する部分との間で大
きな温度差を生じて、補強鉄骨自体に歪みを生ず
るほか、出口ダクト7の底板7aとの相対的移動
により、この底板7aを破損する虞れもある。
<Prior art and its problems> Dry exhaust gas denitrification equipment forms a catalyst layer in the high-temperature boiler exhaust gas flow path, and injects a denitrification agent such as ammonia upstream, thereby reducing the amount of exhaust gas in the exhaust gas as it passes through the catalyst layer. It decomposes nitrogen oxides into water (H 2 O) and nitrogen gas (N 2 ). Among these, the parallel flow type denitrification reactor is a device that incorporates a catalyst layer formed by a plate catalyst, a honeycomb catalyst, etc., and is characterized by a small pressure loss when gas passes through the catalyst layer. For this reason, parallel flow denitrification reactors can be used with existing boilers.
It has the advantage that it can be used by being placed between the outlet of the economizer and the air preheater without installing a new blower or the like. However, since both the economizer and the air preheater are located within the duct of the boiler, the flow direction of the exhaust gas to be introduced into the denitrification reactor must be reversed by 180 degrees at some point. Normally, the flow direction of exhaust gas is reversed in a denitrification reactor, and FIG. 1 shows the structure of an example of a conventional denitrification reactor in which the flow direction of exhaust gas is reversed. The exhaust gas passes through the inlet duct 12 and reaches the denitrification reaction catalyst layer 6.
After passing through, the flow direction is changed by the current plate 8 and reaches the outlet duct 7. In this denitrification reactor, the outlet duct 7 is supported by a reinforcing steel frame 11 that supports the denitrification reaction catalyst layer 6. That is, the reinforcing steel frame 11 supports the upper duct 7 by passing through the ceiling 12a of the lower duct 12 and supporting the bottom plate 7a of the duct 7. However, since a space 14a is formed between the upper duct 7 and the lower duct 12, a large temperature difference occurs between the inside of each duct and this space 14, and there is a risk that the entire denitration reactor may be thermally deformed. . For this reason, in FIG. 1, telescopic members 10a and 10ob for absorbing lateral displacement
Furthermore, in order to absorb displacement in the vertical direction, it is necessary to separately arrange an elastic member 15 at the connection between the lower duct 12 and the upper duct 7, which complicates the overall structure of the device. Furthermore, the reinforcing steel frame 11 also generates a large temperature difference between the inside of the lower duct 12 and the part located in the space 14, causing distortion in the reinforcing steel frame itself, and also due to relative movement with the bottom plate 7a of the outlet duct 7. , there is also a risk of damaging the bottom plate 7a.

<発明の目的> この発明は以上説明した従来技術の欠点をなく
し、脱硝反応器の熱変形が少なく、しかも構造が
簡単な脱硝反応器を提供することにある。
<Objective of the Invention> The object of the present invention is to eliminate the drawbacks of the prior art described above, to provide a denitrification reactor which suffers less thermal deformation and has a simple structure.

<手段の概要> 要するにこの発明は横断面が四角形の入口ダク
トを下側に、横断面が四角形の出口ダクトを上側
に配置し、水平方向変位可能の脚部付き補強鉄骨
で脱硝反応触媒層を支持する脱硝反応器におい
て、前記脱硝反応触媒層の上面と隙間を有し前記
入口ダクトの下流側端部より水平に伸びる仕切板
を前記出口ダクトの底板とし、前記入口ダクトと
出口ダクトを反応器ケーシングで接続し排ガスの
反転流れ流路を形成したことを特徴とする脱硝反
応器である。
<Summary of Means> In short, this invention arranges an inlet duct with a square cross section on the lower side and an outlet duct with a square cross section on the upper side, and uses a reinforced steel frame with horizontally movable legs to support the denitrification reaction catalyst layer. In the supported denitrification reactor, a partition plate having a gap with the upper surface of the denitrification reaction catalyst layer and extending horizontally from the downstream end of the inlet duct is used as the bottom plate of the outlet duct, and the inlet duct and the outlet duct are connected to the reactor. This denitrification reactor is characterized in that it is connected by a casing to form a reverse flow path for exhaust gas.

<実施例> 以下この発明の一実施例を第2図を用いて説明
する。
<Example> An example of the present invention will be described below with reference to FIG.

図において、符号9は排ガス流れを反転流れに
する反応器ケーシングであり、入口ダクトと出口
ダクトを接続している。仕切板13は脱硝反応触
媒層の上面と隙間を有し入口ダクト12aの下流
側端部より水平に伸び出口ダクト7bの底板とな
つている。入口ダクト12a内に脱硝反応触媒層
6を保持する補強鉄骨11aの脚部は水平方向の
変位を自由にし排ガスによる脱硝反応器の部材の
熱膨張があつてもクラツクなどの損傷を生ずるこ
とはない。符号8は排ガスの流れを90゜変向させ
かつ流れの抵抗を少なくし整流をするため設けら
れている。仕切板13は出口ダクトの底板であ
り、かつ入口ダクトの天井板の一部のような形に
なつている。このため第1図の空間部14がない
ので10a,10b,15のような伸縮部材を必
要としない。出口ダクトを出た排ガスはその下流
の空気予熱器へと流れる。
In the figure, reference numeral 9 is a reactor casing that reverses the exhaust gas flow and connects the inlet duct and the outlet duct. The partition plate 13 has a gap with the upper surface of the denitrification reaction catalyst layer, and extends horizontally from the downstream end of the inlet duct 12a, serving as the bottom plate of the outlet duct 7b. The legs of the reinforcing steel frame 11a that holds the denitrification reaction catalyst layer 6 in the inlet duct 12a can be freely displaced in the horizontal direction, so that even if the members of the denitrification reactor undergo thermal expansion due to exhaust gas, no damage such as cracks will occur. . Reference numeral 8 is provided to change the direction of the exhaust gas flow by 90 degrees, reduce flow resistance, and rectify the flow. The partition plate 13 is the bottom plate of the outlet duct, and is shaped like a part of the ceiling plate of the inlet duct. Therefore, since there is no space 14 shown in FIG. 1, there is no need for telescopic members such as 10a, 10b, and 15. Exhaust gas leaving the outlet duct flows downstream to the air preheater.

<発明の効果> この発明を実施することにより、仕切板13
と、脱硝反応触媒層6を支持する水平方向変位可
能な補強鉄骨11aとが使用されているので、熱
応力によるクラツク発生等がなく装置の寿命を延
長できる。
<Effect of the invention> By implementing this invention, the partition plate 13
Since a horizontally movable reinforcing steel frame 11a supporting the denitrification reaction catalyst layer 6 is used, there is no occurrence of cracks due to thermal stress, and the life of the apparatus can be extended.

また入口ダクトと出口ダクトの接合部に伸縮部
材を配置する必要がなく、構造を単純化でき、従
つて製作費も安価に押えることができる。
Furthermore, there is no need to arrange an expandable member at the joint between the inlet duct and the outlet duct, which simplifies the structure and reduces manufacturing costs.

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

第1図は従来のパラレルフロー式脱硝装置の側
断面図、第2図はこの発明の一実施例に係る脱硝
反応器の側断面図である。 6……脱硝反応触媒層、9……反応器ケーシン
グ、11,11a……補強鉄骨、12,12a…
…入口ダクト、13……仕切板。
FIG. 1 is a side sectional view of a conventional parallel flow type denitrification apparatus, and FIG. 2 is a side sectional view of a denitrification reactor according to an embodiment of the present invention. 6... Denitrification reaction catalyst layer, 9... Reactor casing, 11, 11a... Reinforced steel frame, 12, 12a...
...Inlet duct, 13...Partition plate.

Claims (1)

【特許請求の範囲】[Claims] 1 横断面が四角形の入口ダクトを下側に、横断
面が四角形の出口ダクトを上側に配置し、水平方
向変位可能の脚部付き補強鉄骨で脱硝反応触媒層
を支持する脱硝反応器において、前記脱硝反応触
媒層の上面と隙間を有し前記入口ダクトの下流側
端部より水平に伸びる仕切板を前記出口ダクトの
底板とし、前記入口ダクトと出口ダクトを反応器
ケーシングで接続し排ガスの反転流れ流路を形成
したことを特徴とする脱硝反応器。
1. In a denitrification reactor in which an inlet duct with a square cross section is disposed on the lower side, an outlet duct with a square cross section is arranged on the upper side, and a denitrification reaction catalyst layer is supported by a reinforced steel frame with horizontally displaceable legs, A partition plate that has a gap with the upper surface of the denitrification reaction catalyst layer and extends horizontally from the downstream end of the inlet duct serves as the bottom plate of the outlet duct, and the inlet and outlet ducts are connected by a reactor casing to prevent the reverse flow of exhaust gas. A denitrification reactor characterized by forming a flow path.
JP15251079A 1979-11-27 1979-11-27 Parallel flow type denitration reactor Granted JPS5676226A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15251079A JPS5676226A (en) 1979-11-27 1979-11-27 Parallel flow type denitration reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15251079A JPS5676226A (en) 1979-11-27 1979-11-27 Parallel flow type denitration reactor

Publications (2)

Publication Number Publication Date
JPS5676226A JPS5676226A (en) 1981-06-23
JPH025445B2 true JPH025445B2 (en) 1990-02-02

Family

ID=15542022

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15251079A Granted JPS5676226A (en) 1979-11-27 1979-11-27 Parallel flow type denitration reactor

Country Status (1)

Country Link
JP (1) JPS5676226A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6039325U (en) * 1983-08-25 1985-03-19 三菱重工業株式会社 Denitration equipment

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5531207Y2 (en) * 1975-10-18 1980-07-25

Also Published As

Publication number Publication date
JPS5676226A (en) 1981-06-23

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