JPS5935656B2 - Catalyst unit for exhaust gas denitrification equipment - Google Patents
Catalyst unit for exhaust gas denitrification equipmentInfo
- Publication number
- JPS5935656B2 JPS5935656B2 JP51079149A JP7914976A JPS5935656B2 JP S5935656 B2 JPS5935656 B2 JP S5935656B2 JP 51079149 A JP51079149 A JP 51079149A JP 7914976 A JP7914976 A JP 7914976A JP S5935656 B2 JPS5935656 B2 JP S5935656B2
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- exhaust gas
- catalyst unit
- double
- porous
- 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
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【発明の詳細な説明】
本発明は窒素酸化物(以下、NOxという)を含む燃焼
排ガス(以下、単に排ガスという)を処理する排煙脱硝
装置用の触媒ユニットに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a catalyst unit for a flue gas denitrification device that processes combustion exhaust gas (hereinafter simply referred to as exhaust gas) containing nitrogen oxides (hereinafter referred to as NOx).
排ガス中のNOxを分解、除去するために、NH3、H
2S、H2、CO、CH4などの還元剤を排ガスに添加
し、触媒と接触させてN0xをN2にまで還元する、い
わゆる乾式排煙脱硝装置が最近開発されつつある。しか
し上記従来の装置における脱硝反応器は、反応器本体内
に触媒を投入・落下させて単に充填した構造のものが一
般的であり、このため落下による触媒の分散、衝撃・衝
突による触媒の破損が多い上に、触媒層を一定の厚さに
保持するのが困難であり、また触媒の投入、抜出しに手
間がかかるという欠点を有していた。In order to decompose and remove NOx in exhaust gas, NH3, H
Recently, so-called dry flue gas denitrification equipment has been developed, in which a reducing agent such as 2S, H2, CO, CH4, etc. is added to the exhaust gas and brought into contact with a catalyst to reduce NOx to N2. However, the denitrification reactor in the conventional equipment described above generally has a structure in which the catalyst is simply put in and dropped into the reactor body, and as a result, the catalyst is dispersed due to falling, and the catalyst is damaged due to impact and collision. In addition, it is difficult to maintain the catalyst layer at a constant thickness, and it is time-consuming to add and remove the catalyst.
本発明は上記の欠点を解消するためになされたもので、
側部内面および側部外面に広い面積の側部開口部を有す
る筒状枠体のこの側部開口部に、金網または金属製多孔
板のような多孔体を取り付けて二重多孔筒体を形成する
とともに、この二重多孔筒体内に脱硝触媒を充填し、さ
らに二重多孔筒体の下部に別の二重多孔筒体の上部開口
部に嵌合して積重ね自在の接続筒を設けることにより、
触媒を保護して落下による分散、衝撃・衝突による破損
を少なくし、かつ触媒層を一定の厚さに保持し、しかも
均等重量物として取扱いが容易で十分な安定性を保つて
容易に積み重ねることができる排煙脱硝装置用の触媒ユ
ニットの提供を目的とするものである。The present invention has been made to solve the above-mentioned drawbacks.
A porous body such as a wire mesh or a perforated metal plate is attached to the side openings of a cylindrical frame having wide area side openings on the inner side surface and the outer side surface to form a double porous cylinder body. At the same time, by filling this double-porous cylinder with a denitrification catalyst, and further providing a connecting cylinder at the bottom of the double-porous cylinder that can be stacked by fitting into the upper opening of another double-porous cylinder. ,
To protect the catalyst and reduce its dispersion due to falling and damage due to impact/collision, to maintain the catalyst layer at a constant thickness, and to be easy to handle as a uniformly weighted object and to maintain sufficient stability so that it can be stacked easily. The purpose of the present invention is to provide a catalyst unit for an exhaust gas denitrification device that can perform the following steps.
以下、本発明の構成を図面に示す実施例に基づいて説明
する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The structure of the present invention will be described below based on embodiments shown in the drawings.
第1図および第2図は本発明の一実施例における触媒ユ
ニット1を示す。2は金属製枠材からなる円筒状枠体で
、この円筒状枠体2は側部内面および側部外面に広い面
積の側部内面開口部3および側部外面開口部4を有して
いる。1 and 2 show a catalyst unit 1 in one embodiment of the present invention. Reference numeral 2 denotes a cylindrical frame body made of metal frame material, and this cylindrical frame body 2 has a wide area inner side opening 3 and side outer opening 4 on the inner side surface and the outer side surface. .
これらの開口部3、4に金網5を溶接などにより固着し
て取り付けて二重多孔筒体6を形成する。さらに二重多
孔筒体6の下部に別の二重多孔筒体の上部開口部に嵌合
して積重ね自在の短かい接続筒7を取り付ける。前記円
筒状枠体2の上面には触媒投入口8が穿設されており、
この触媒投入口から、二重多孔筒体内にペレツト状、柱
状、ラシヒリング状などの脱硝触媒10を充填して、一
定厚さでかつ一定重量を有する触媒ユニツト1を構成す
る。なお円筒状枠体2の上面には吊金具(図示せず)が
固着される。また金網の代りに金属製多孔板を用いても
差し支えない。第3図は本発明の触媒ユニツトの他の実
施例を示している。A double porous cylindrical body 6 is formed by firmly attaching a wire mesh 5 to these openings 3 and 4 by welding or the like. Furthermore, a short connecting tube 7 that can be freely stacked is attached to the lower part of the double-porous cylinder 6 by fitting into the upper opening of another double-porous cylinder. A catalyst inlet 8 is bored in the upper surface of the cylindrical frame 2,
A denitration catalyst 10 in the form of pellets, columns, Raschig rings, etc. is filled into the double porous cylinder through this catalyst inlet to form a catalyst unit 1 having a constant thickness and constant weight. Note that a hanging fitting (not shown) is fixed to the upper surface of the cylindrical frame 2. Also, a perforated metal plate may be used instead of the wire mesh. FIG. 3 shows another embodiment of the catalyst unit of the invention.
本実施例における触媒ユニツト11は、四角筒状枠体1
2の側部開口部に多孔体13を取り付けて二重多孔筒体
14を形成するとともに、この二重多孔筒体内に脱硝触
媒10を充填し、さらに二重多孔筒体14の下部に接続
筒15を設けたものである。他の構成は前記の実施例の
場合と同様である。なお触媒ユニツトの形状を円筒状、
四角筒状とする代りに、多角筒状とすることも可能であ
る。The catalyst unit 11 in this embodiment has a square cylindrical frame 1
A porous body 13 is attached to the side opening of the double-porous cylinder 14 to form a double-porous cylinder 14, and a denitrification catalyst 10 is filled in the double-porous cylinder. 15. The other configurations are the same as in the previous embodiment. The shape of the catalyst unit is cylindrical,
Instead of a square cylinder shape, it is also possible to use a polygonal cylinder shape.
上記のように構成された触媒ユニツトは、第4図に示す
ように反応体16内に収納・配置される。この反応器本
体16は一端の下側部に排ガス入口17を、他端の上側
部に清浄ガス出口18を有しており、反応器本体16内
の排ガス通路の上側に盲板20を設け、この盲板に触媒
ユニツト下部の接続筒7,15を嵌合自在の孔を穿設し
てこの孔に接続筒7,15を嵌合して触媒ユニツト1,
11を取り付ける。さらにこの触媒ユニツトに順次、別
の触媒ユニツトを積み重ねた後、最上部の触媒ユニツト
の上部開口部に盲板21を取り付ける。したがつて反応
器本体16内に導入された排ガス(既に還元剤が添加さ
れている)は、触媒ユニツト1,11の内部から外部へ
流過し、この際触媒と接触して排ガス中のNOxがN2
に分解して無害化され、清浄ガス出口18から排出され
る。この場合の反応式を一例としてアンモニアを還元剤
として用いた場合について記載するとつぎの如くである
。つぎに触媒ユニツトの配置例を第5図〜第8図に基づ
いて説明する。The catalyst unit constructed as described above is housed and arranged within the reactor 16 as shown in FIG. This reactor body 16 has an exhaust gas inlet 17 at the lower side of one end and a clean gas outlet 18 at the upper side of the other end, and a blind plate 20 is provided above the exhaust gas passage in the reactor body 16. A hole is bored in this blind plate into which the connection cylinders 7 and 15 at the lower part of the catalyst unit can be fitted, and the connection cylinders 7 and 15 are fitted into the hole to form the catalyst unit 1,
Attach 11. Further, after another catalyst unit is successively stacked on top of this catalyst unit, a blind plate 21 is attached to the upper opening of the uppermost catalyst unit. Therefore, the exhaust gas introduced into the reactor main body 16 (to which a reducing agent has already been added) flows from the inside of the catalyst units 1, 11 to the outside, and at this time comes into contact with the catalyst to reduce NOx in the exhaust gas. is N2
The gas is decomposed and rendered harmless, and is discharged from the clean gas outlet 18. The reaction formula in this case is as follows, as an example, when ammonia is used as the reducing agent. Next, an example of the arrangement of the catalyst unit will be explained based on FIGS. 5 to 8.
まず第5図は、反応器本体16内に触媒ユニツト11の
角部同志が隣接するように配置する場合を示している。
22は断面十字状のガイド柱、23は排ガス煙道、24
は清浄ガス煙道である。First, FIG. 5 shows a case where the catalyst units 11 are arranged in the reactor main body 16 so that the corner portions of the catalyst units 11 are adjacent to each other.
22 is a guide column with a cross-shaped cross section, 23 is an exhaust gas flue, 24
is a clean gas flue.
触媒ユニツトの角部は枠材を有しているため排ガス流過
しないので、第6図に示すように角部の枠材の部分をオ
ーバラツプさせて、反応器本体内の空間を有効に利用す
るように配置するのが望ましい。25はZ形鋼のような
断面略Z字状のガイド柱である。Since the corners of the catalyst unit have frame materials, exhaust gas does not flow through them, so the frame materials at the corners are overlapped as shown in Figure 6 to effectively utilize the space inside the reactor body. It is desirable to arrange it as follows. Reference numeral 25 indicates a guide column having a substantially Z-shaped cross section, such as a Z-shaped steel.
また第7図に示すように、触媒ユニツトを四角配列する
こともあり、さらに第8図に示すように触媒ユニツトを
三角配列することもある。26は山形鋼のような断面略
L字状のガイド柱である。Further, as shown in FIG. 7, the catalyst units may be arranged in a square arrangement, and as shown in FIG. 8, the catalyst units may be arranged in a triangular arrangement. Reference numeral 26 indicates a guide column having a substantially L-shaped cross section, such as made of angle iron.
なお触媒ユニツトの配置は第5図〜第8図に示す配置例
に限ることなく、反応器本体の大きさ・形状、触媒ユニ
ツトの大きさ・形状などに応じて適宜選択することがで
きる。以上説明したように、本発明の排煙脱硝装置用の
触媒ユニツトは、均等重量物として挿入、取出しなど取
扱いがきわめて容易でかつ十分な安定性を保つて容易に
積み重ねることができる。また触媒層の厚みを一定に保
持することができる上に、触媒が保護されているので、
従来のような落下による分散、衝撃・衝突による破損が
少なくなる。また複数個の触媒ユニツトを組み合わせる
ことにより、各種の配列が可能であるなどの効果を有し
ている。Note that the arrangement of the catalyst units is not limited to the arrangement examples shown in FIGS. 5 to 8, and can be appropriately selected depending on the size and shape of the reactor body, the size and shape of the catalyst units, etc. As explained above, the catalyst unit for the exhaust gas denitrification apparatus of the present invention is extremely easy to handle as an object of equal weight, such as insertion and removal, and can be easily stacked while maintaining sufficient stability. In addition, the thickness of the catalyst layer can be maintained constant, and the catalyst is protected, so
Dispersion due to falling and damage due to impact/collision, which is the case with conventional products, is reduced. Furthermore, by combining a plurality of catalyst units, various arrangements are possible.
第1図は本発明の排煙脱硝装置用の触媒ユニツトの一実
施例を示す斜視図、第2図は同縦断面図、第3図は触媒
ユニツトの他の実施例を示す斜視図、第4図は本発明の
触媒ユニツトを有する排煙脱硝装置反応器の説明図、第
5図〜第8図は本発明の触媒ユニツトの配置例を示す説
明図である。
1,11・・・・−・触媒ユニツト、2・・・・・・円
筒状枠体、3・・・・・・側部内面開口部、4・・・・
・・側部外面開口部、5・・・・・・金網、6,14・
・・・・・二重多孔筒体、7,15・・・・・・接続筒
、8・・・・・・触媒投入口、10・・・・・・脱硝触
媒、12・・・・・・四角筒状枠体、13・・・・・・
多孔体、16・・・・・・反応器本体、17・・・・・
・排ガス入口、18・・・・・・清浄ガス出口、20,
21・・・・・・盲板、22,25,26・・・・・・
ガイド柱、23・・・・・・排ガス煙道、24・・・・
・・清浄ガス煙道。FIG. 1 is a perspective view showing one embodiment of a catalyst unit for an exhaust gas denitrification device of the present invention, FIG. 2 is a longitudinal cross-sectional view of the same, and FIG. 3 is a perspective view showing another embodiment of the catalyst unit. FIG. 4 is an explanatory diagram of a flue gas denitrification apparatus reactor having a catalyst unit of the present invention, and FIGS. 5 to 8 are explanatory diagrams showing examples of arrangement of the catalyst unit of the present invention. 1, 11... Catalyst unit, 2... Cylindrical frame, 3... Side inner surface opening, 4...
... Side external opening, 5 ... Wire mesh, 6, 14.
...Double porous cylinder, 7, 15... Connection pipe, 8... Catalyst inlet, 10... Denitrification catalyst, 12...・Square cylindrical frame, 13...
Porous body, 16...Reactor body, 17...
・Exhaust gas inlet, 18...Clean gas outlet, 20,
21...Blind board, 22, 25, 26...
Guide column, 23...Exhaust gas flue, 24...
・Clean gas flue.
Claims (1)
有する筒状枠体のこの側部開口部に、多孔体を取り付け
て二重多孔筒体を形成するとともに、この二重多孔筒体
内に脱硝触媒を充填し、さらに二重多孔筒体の下部に別
の二重多孔筒体の上部開口部に嵌合して積重ね自在の接
続筒を設けたことを特徴とする排煙脱硝装置用の触媒ユ
ニット。1 A porous body is attached to the side opening of a cylindrical frame having a wide area on the inner surface and outer surface of the side to form a double-porous cylinder, and this double-porous cylinder is A flue gas denitrification device, characterized in that a denitrification catalyst is filled inside the body, and a connecting cylinder is provided at the bottom of the double-porous cylinder so that it can be stacked freely by fitting into the upper opening of another double-porous cylinder. Catalyst unit for.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51079149A JPS5935656B2 (en) | 1976-07-03 | 1976-07-03 | Catalyst unit for exhaust gas denitrification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51079149A JPS5935656B2 (en) | 1976-07-03 | 1976-07-03 | Catalyst unit for exhaust gas denitrification equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS534767A JPS534767A (en) | 1978-01-17 |
| JPS5935656B2 true JPS5935656B2 (en) | 1984-08-30 |
Family
ID=13681892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51079149A Expired JPS5935656B2 (en) | 1976-07-03 | 1976-07-03 | Catalyst unit for exhaust gas denitrification equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5935656B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104275127A (en) * | 2013-07-02 | 2015-01-14 | 中国石油化工股份有限公司 | Dirt-capturing basket and usage method thereof |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59138440U (en) * | 1983-03-07 | 1984-09-14 | 株式会社新潟鐵工所 | Cartridge type packed bed |
| JP7235382B2 (en) * | 2018-06-19 | 2023-03-08 | 株式会社豊田中央研究所 | Reactor |
-
1976
- 1976-07-03 JP JP51079149A patent/JPS5935656B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104275127A (en) * | 2013-07-02 | 2015-01-14 | 中国石油化工股份有限公司 | Dirt-capturing basket and usage method thereof |
| CN104275127B (en) * | 2013-07-02 | 2016-06-29 | 中国石油化工股份有限公司 | Catch dirt basket and using method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS534767A (en) | 1978-01-17 |
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