JPS592833Y2 - Moving bed type denitrification equipment for sintering furnace exhaust gas - Google Patents

Moving bed type denitrification equipment for sintering furnace exhaust gas

Info

Publication number
JPS592833Y2
JPS592833Y2 JP1977037530U JP3753077U JPS592833Y2 JP S592833 Y2 JPS592833 Y2 JP S592833Y2 JP 1977037530 U JP1977037530 U JP 1977037530U JP 3753077 U JP3753077 U JP 3753077U JP S592833 Y2 JPS592833 Y2 JP S592833Y2
Authority
JP
Japan
Prior art keywords
exhaust gas
wire mesh
main body
denitrification
moving 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
Application number
JP1977037530U
Other languages
Japanese (ja)
Other versions
JPS53132944U (en
Inventor
俊一 水上
Original Assignee
工業技術院長
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 工業技術院長 filed Critical 工業技術院長
Priority to JP1977037530U priority Critical patent/JPS592833Y2/en
Publication of JPS53132944U publication Critical patent/JPS53132944U/ja
Application granted granted Critical
Publication of JPS592833Y2 publication Critical patent/JPS592833Y2/en
Expired legal-status Critical Current

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【考案の詳細な説明】 本考案は焼結炉排ガス用移動層式脱硝装置に関する。[Detailed explanation of the idea] The present invention relates to a moving bed type denitrification device for sintering furnace exhaust gas.

従来、焼結炉排ガスの乾式脱硝装置としては一般に固定
床方式が採用されていたが、排ガス中に含まれるダスト
の性状が原因で触媒層中へのダストの付着が著るしく、
長期的な連続運転が困難であった。
Conventionally, a fixed bed method was generally used as a dry denitrification device for sintering furnace exhaust gas, but due to the nature of the dust contained in the exhaust gas, the dust adhered to the catalyst layer significantly.
Long-term continuous operation was difficult.

そこで上記問題を解決するため、粒、状触媒を排ガス流
路中を移動させる移動層方式の脱硝装置が考案されたが
、この移動層方式のものにおいても、触媒を保持する金
網のうち排ガス流路の上流側に位置する金網にダストが
付着する現象はいかなる形状の金網を使用しても不可避
であり、そのため長期運転中には徐々に圧力損失が増大
し、その結果脱硝装置としての処理能力を維持すること
が不可能となる。
Therefore, in order to solve the above problem, a moving bed denitrification device was devised in which catalyst particles are moved through the exhaust gas flow path, but even in this moving bed method, the wire mesh that holds the catalyst is The phenomenon of dust adhering to the wire mesh located on the upstream side of the channel is unavoidable no matter what shape of wire mesh is used.As a result, pressure loss gradually increases during long-term operation, resulting in a reduction in the processing capacity of the denitrification equipment. becomes impossible to maintain.

斜上に鑑み、本考案は、上記移動層式脱硝装置において
、上流側の金網をハンマリングして付着したダストを除
去するハンマリング装置を設けることにより、該脱硝装
置の安定的な処理能力を維持した状態での長期的な運転
を可能ならしめたことをその特徴とするものである。
In view of the above problem, the present invention improves the stable processing capacity of the moving bed denitrification equipment by providing a hammering device that hammers the wire mesh on the upstream side and removes the attached dust. Its feature is that it enables long-term operation under maintained conditions.

以下、本考案の実施例を図面に基すいて詳細に説明する
に、第1図において1は脱硝装置の本体であって処理す
べき排ガスの流入口2と処理された排ガスの流出口3と
を有し、該本体1の中央には、上記流入口2から流出口
3に至る排ガス流路4と交叉してそれを縦断する脱硝触
媒の移送路5を形成すると共に、該移送路5の排ガス流
路4との交叉部における上流側の側面及び下流側の側面
にそれぞれ触媒の保持と排ガスの流通とが可能な適宜の
金網6,7を張設し、また該移送路5の上下端には触媒
の供給口8及び排出口9を設けている。
Hereinafter, embodiments of the present invention will be explained in detail with reference to the drawings. In Fig. 1, 1 is the main body of the denitrification equipment, which has an inlet 2 for the exhaust gas to be treated and an outlet 3 for the treated exhaust gas. In the center of the main body 1, there is formed a denitrification catalyst transfer path 5 that intersects and traverses the exhaust gas flow path 4 from the inlet 2 to the outlet 3, and a denitrification catalyst transfer path 5 is formed in the center of the main body 1. Appropriate wire meshes 6 and 7 capable of holding the catalyst and distributing the exhaust gas are installed on the upstream and downstream sides of the intersection with the exhaust gas flow path 4, respectively, and the upper and lower ends of the transfer path 5 is provided with a catalyst supply port 8 and a catalyst discharge port 9.

上記上流側の金網6をハンマリングするためのハンマリ
ング装置10は、第2図及び第3図から明らかなように
、本体1の側面の支持台11上に軸受12によって回転
自在に支承された軸棒13の一端に、金網6に添設した
座14に衝突するハンマ15の支持アーム16を固定す
ると共に、該軸棒13の基部に多数の円板状のウエート
17を増減可能に取付けたウエートアーム18を固定し
、該ウエートアーム18の他端にはカムフォロア19を
形設してそれを軸受20により回転自在に支持されたカ
ム軸21上のカム22に対向さセ、該カム軸21の他端
にはスプロケット23を固定して該スプロケット23と
本体1上に配設した減速機付モータ24のスプロケット
25との間にチ土−ン26を巻掛けている。
As is clear from FIGS. 2 and 3, the hammering device 10 for hammering the wire mesh 6 on the upstream side is rotatably supported by a bearing 12 on a support stand 11 on the side surface of the main body 1. A support arm 16 of a hammer 15 that collides with a seat 14 attached to a wire mesh 6 is fixed to one end of the shaft rod 13, and a large number of disc-shaped weights 17 are attached to the base of the shaft rod 13 so that they can be increased or decreased. A weight arm 18 is fixed, a cam follower 19 is formed at the other end of the weight arm 18, and the cam follower 19 is opposed to a cam 22 on a cam shaft 21 rotatably supported by a bearing 20. A sprocket 23 is fixed to the other end, and a chain 26 is wound between the sprocket 23 and a sprocket 25 of a motor 24 with a reduction gear disposed on the main body 1.

上記構成を有する移動層式脱硝装置においては、流入口
2から流路4内に流入した排ガスは上流側の金網6の網
目を通って触媒の移送路5内に流入し、こ・で該移送路
5内を下方に移送される触媒層中を通過する間に該触媒
と接触して脱硝処理され、下流側の金網7から再び流路
4中に抜けて流出口3から流出する。
In the moving bed type denitrification apparatus having the above configuration, the exhaust gas that has flowed into the flow path 4 from the inlet 2 passes through the mesh of the wire mesh 6 on the upstream side and flows into the catalyst transfer path 5. While passing through the catalyst layer transferred downward in the channel 5, it comes into contact with the catalyst and undergoes denitrification treatment, passes through the wire mesh 7 on the downstream side into the channel 4 again, and flows out from the outlet 3.

このとき排ガス中に含まれるダストは、排ガスが上流側
の金網6を通して移送路5に流入する際、該金網6によ
り一部が濾過されてその表面に付着し、その付着量の増
加に伴なって流路4における圧力損失は次第に増大する
At this time, when the exhaust gas flows into the transfer path 5 through the wire mesh 6 on the upstream side, a part of the dust contained in the exhaust gas is filtered by the wire mesh 6 and adheres to the surface thereof, and as the amount of dust attached increases. As a result, the pressure loss in the flow path 4 gradually increases.

そこで、定期的あるいは圧力損失が一定値に達したとき
に、自動的あるいは外部操作によりハンマリング装置1
0を作動させることにより、付着ダストの除去を行うこ
とができる。
Therefore, periodically or when the pressure loss reaches a certain value, the hammering device 1 is automatically or externally operated.
By operating 0, the attached dust can be removed.

即ち、モータ24を駆動するとチェーン26を介してカ
ム軸21が回転し、その一端に固定したカム22が回動
してカムフォロア19を押し下げるため軸棒13が回転
してウエート17及びハンマ15が第1図に示す鎖線位
置まで持ち上げられる。
That is, when the motor 24 is driven, the cam shaft 21 rotates via the chain 26, and the cam 22 fixed to one end of the cam shaft 22 rotates to push down the cam follower 19, causing the shaft rod 13 to rotate and the weight 17 and the hammer 15 to rotate. It is lifted up to the position indicated by the chain line shown in Figure 1.

そして、更にカム22が回動してカムフォロア19から
外れると、ウエート17はその重力により鎖線位置から
降下し、同時にハンマ15も降下してウエート17の重
量に応じた衝撃力をもって金網6の座14に衝突する。
Then, when the cam 22 rotates further and comes off the cam follower 19, the weight 17 descends from the chain line position due to its gravity, and at the same time, the hammer 15 also descends and applies an impact force corresponding to the weight of the weight 17 to the seat 14 of the wire mesh 6. collide with

この時の金網6の振動により付着したダストは剥離し、
その一部は装置下部に落下して振動篩(図示せず)から
排出され、残りは排ガスと共に触媒層中を通り抜けて被
処理ガスと共に排出される。
At this time, the attached dust is peeled off due to the vibration of the wire mesh 6,
A part of it falls to the bottom of the apparatus and is discharged from a vibrating sieve (not shown), and the rest passes through the catalyst layer together with the exhaust gas and is discharged together with the gas to be treated.

このようにして、金網6へのダストの付着量が増大する
毎にハンマリング装置10を作動させてその除去を行い
、それによって装置の長期連続運転を行うものである。
In this way, the hammering device 10 is operated to remove the dust each time the amount of dust adhering to the wire mesh 6 increases, thereby allowing the device to operate continuously for a long period of time.

上記ハンマ15による衝撃力はウェー1〜17の増減に
より任意に調節することができる。
The impact force by the hammer 15 can be arbitrarily adjusted by increasing or decreasing the number of wafers 1 to 17.

第4図は本考案者らがテスト装置により焼却炉の実ガス
を用いて行なった実験結果を示すものである。
FIG. 4 shows the results of an experiment conducted by the present inventors using a test device using actual gas from an incinerator.

同図から明らかなように、テスト装置における触媒層の
初期の圧力損失は約4Q mmAqであったが、約20
0時間経過後に急激に上昇し始めた。
As is clear from the figure, the initial pressure loss of the catalyst layer in the test device was about 4Q mmAq, but it was about 20Q mmAq.
After 0 hours, it started to rise rapidly.

そこで、圧力損失が5Q mmAq程度になった時点で
脱硝装置の運転を続行しながらハンマリングを行なった
ところ、その圧力損失は初期の値に回復した。
Therefore, when the pressure loss reached approximately 5Q mmAq, hammering was performed while the denitration equipment continued to operate, and the pressure loss recovered to its initial value.

なお、ハンマリングによる触媒の破損は皆無であった。Note that there was no damage to the catalyst due to hammering.

この実験結果から、ハンマリングの頻度をさらに増加す
ることにより常に初期状態の圧力損失(4QmmAq程
度)で装置を運転できることは明らかである。
From the results of this experiment, it is clear that by further increasing the frequency of hammering, the device can always be operated with the initial pressure loss (approximately 4 QmmAq).

このように本考案の脱硝装置によれば、ハンマ1ング装
置を設けたので金網に付着したダストの除去を極めて簡
単且つ確実に行うことができ、しかもその除去は、装置
の運転中においてもダストが付着する度に簡単に行うこ
とができ、そのため該脱硝装置を排ガスの処理能力を安
定的に維持した状態で長期的に連続運転することができ
る等の勝れた特徴がある。
As described above, according to the denitrification device of the present invention, since the hammering device is provided, the dust attached to the wire mesh can be removed extremely easily and reliably, and furthermore, the dust can be removed even during operation of the device. This method has excellent features such as being able to easily carry out the denitrification process each time the denitrification device is deposited, and therefore, the denitrification device can be operated continuously for a long period of time while stably maintaining the exhaust gas treatment capacity.

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

第1図は本考案に係る脱硝装置の概略縦断面図、第2図
はその要部拡大正面図、第3図は同要部拡大側面図、第
4図はテスト装置による実験結果を示す線図である。 1・・・・・・本体、4・・・・・・排ガス流路、5・
・・・・・触媒移送路、6.7・・・・・・金網、10
・・・・・・ハンマリング装置、15・・・・・・ハン
マ。
Fig. 1 is a schematic vertical cross-sectional view of the denitrification device according to the present invention, Fig. 2 is an enlarged front view of its main parts, Fig. 3 is an enlarged side view of the main parts, and Fig. 4 is a line showing experimental results using a test device. It is a diagram. 1...Main body, 4...Exhaust gas flow path, 5.
... Catalyst transfer path, 6.7 ... Wire mesh, 10
... Hammering device, 15 ... Hammer.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 脱硝装置本体内に脱硝処理すべき排ガスの流路とそれと
交叉する脱硝用触媒の移送路とを形成すると共に、該移
送路の排ガスとの交叉部における排ガスの上流側及び下
流側の側面にそれぞれ触媒の保持と排ガスの流通とが可
能な金網を張設し、上記脱硝装置本体には、排ガスの上
流側の金網に添着した座をハンマリングするためのハン
マを有するハンマリング装置を配設したものからなり、
該ハンマリング装置は、前記本体の側面の支体台上に軸
受によって回転自在に支承された軸棒の一端に、金網に
添設した座に衝突するハンマの支持アームを固定すると
共に、該軸棒の基部に多数の円板状のウエートを増減可
能に取付けたウエートアームを固定し、該ウエートアー
ムの他端にはカムフォロアを形設してそれを軸受により
回転自在に支持されたカム軸上のカムに対向させ、該カ
ム軸の他端にはスプロケットを固定して該スプロケット
と本体上に配設した減速機付モータのスプロケットとの
間にチェーンを巻付けたものから構成されることを特徴
とする焼結炉排ガス用移動層式
A flow path for the exhaust gas to be denitrified and a transfer path for the denitrification catalyst that intersects with the flow path for the exhaust gas to be denitrified are formed in the denitrification device main body, and a flow path for the exhaust gas is formed on the upstream and downstream sides of the exhaust gas at the intersection of the transfer path with the exhaust gas. A wire mesh capable of holding the catalyst and circulating exhaust gas is installed, and a hammering device having a hammer for hammering a seat attached to the wire mesh on the upstream side of the exhaust gas is installed in the denitrification device main body. Consisting of things,
In this hammering device, a support arm of a hammer that collides with a seat attached to a wire mesh is fixed to one end of a shaft rod rotatably supported by a bearing on a support base on the side of the main body, and A weight arm is fixed to the base of a rod, and a cam follower is formed at the other end of the weight arm. A sprocket is fixed to the other end of the camshaft, and a chain is wound between the sprocket and the sprocket of a motor with a reduction gear installed on the main body. Characteristic moving bed type for sintering furnace exhaust gas
JP1977037530U 1977-03-28 1977-03-28 Moving bed type denitrification equipment for sintering furnace exhaust gas Expired JPS592833Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1977037530U JPS592833Y2 (en) 1977-03-28 1977-03-28 Moving bed type denitrification equipment for sintering furnace exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1977037530U JPS592833Y2 (en) 1977-03-28 1977-03-28 Moving bed type denitrification equipment for sintering furnace exhaust gas

Publications (2)

Publication Number Publication Date
JPS53132944U JPS53132944U (en) 1978-10-21
JPS592833Y2 true JPS592833Y2 (en) 1984-01-26

Family

ID=28900756

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1977037530U Expired JPS592833Y2 (en) 1977-03-28 1977-03-28 Moving bed type denitrification equipment for sintering furnace exhaust gas

Country Status (1)

Country Link
JP (1) JPS592833Y2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6053322U (en) * 1983-09-20 1985-04-15 川崎重工業株式会社 Clogging removal device for moving particle holding plate with multiple moving layers
AT411264B (en) * 2002-02-14 2003-11-25 Voest Alpine Ind Anlagen DISTRIBUTOR FLOOR FOR DISTRIBUTING A GAS LOADED WITH FINE SOLID PARTICLES
JP6836168B2 (en) * 2017-03-29 2021-02-24 中国電力株式会社 Denitration device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51137440U (en) * 1975-04-28 1976-11-06

Also Published As

Publication number Publication date
JPS53132944U (en) 1978-10-21

Similar Documents

Publication Publication Date Title
EP0563154B1 (en) Filter cleaning apparatus
US6232254B1 (en) Method of cleaning and/or regenerating wholly or partially de-activated catalysts for stack-gas nitrogen scrubbing
JPS592833Y2 (en) Moving bed type denitrification equipment for sintering furnace exhaust gas
EP2913091B1 (en) Method for cleaning a fabric filter system
US4548623A (en) Perforated trough conditioning device
CN113976427B (en) Dust removal type vibration concentrating machine capable of cleaning screen
CN208599245U (en) Effluent filter
CN208959502U (en) A kind of bag filter
CN108411306A (en) A kind of copper surface chemical polishing processing system
CN114950025B (en) Zinc smoke dust collector in hot galvanizing technology
JP4323960B2 (en) Distributor base for distributing gas loaded with fine solid particles
CN218130584U (en) Fold formula sack pulse dust collector
JPH08224424A (en) Dust collector
JPH06334A (en) Filter for dust removal and denitration
CN209196860U (en) A kind of incineration treatment of garbage dust-extraction unit
CN108310868B (en) Pulse dust removal unloads grey equipment
US4780993A (en) Method and apparatus for surface treating a workpiece
CN208161226U (en) A kind of bag filter
AU592850B2 (en) Periodic action device for filtration of fluid medium
JPS5932177B2 (en) gas treatment equipment
JP2597079B2 (en) Cleaning device for centrifugal molding tunnel liner form lid
CN221035725U (en) Ash removal device for fluidized bed boiler
JPH01501850A (en) stacked fiber recirculation filter
JPH01119343A (en) Reactivation treatment of denitrated catalyst
JP3012150B2 (en) Louver cleaning method for reaction tower inlet