JPH0226620A - Dust removing device of denitrification apparatus - Google Patents
Dust removing device of denitrification apparatusInfo
- Publication number
- JPH0226620A JPH0226620A JP63173951A JP17395188A JPH0226620A JP H0226620 A JPH0226620 A JP H0226620A JP 63173951 A JP63173951 A JP 63173951A JP 17395188 A JP17395188 A JP 17395188A JP H0226620 A JPH0226620 A JP H0226620A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- damper
- hinge type
- removing device
- dust removing
- 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.)
- Granted
Links
- 239000000428 dust Substances 0.000 title claims abstract description 23
- 239000003054 catalyst Substances 0.000 claims abstract description 41
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 4
- 238000010276 construction Methods 0.000 abstract 2
- 239000007789 gas Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は脱硝装置における触媒充填部のダスト付着によ
る機能低下及び圧力損失上昇を防止するためのダスト除
去装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a dust removal device for preventing functional deterioration and pressure loss increase due to dust adhesion to a catalyst-packed portion of a denitrification device.
脱硝装置における触媒充填部に付着したダストを除去す
る従来の一態様を、第6図によって説明する。この態様
はガス縦流れの場合を示すもので、脱硝装置は脱硝反応
器1の中に触媒支持部材3により触媒2が支持内蔵され
ている。A conventional method for removing dust attached to a catalyst filling part in a denitrification device will be explained with reference to FIG. 6. This embodiment shows the case of vertical gas flow, and the denitrification device has a catalyst 2 supported and built in a denitrification reactor 1 by a catalyst support member 3.
入口排ガス4は触媒2の上部から入シ触媒部を垂直に流
れ出口排ガス5となるが、触媒2上方でガス通路を分割
し、かつ、触媒通過ガスの分割性(触媒との間隔を極力
小さくして、分割した他方の通路のガスのもれ込みを極
力少なくする)をよくするように配置を工夫した仕切板
11を設け、仕切板11によって形成される各々のガス
通路内にバタフライダンパ9 10が支点6によって支
持設置されている。なお、第6図中、点線はバタフライ
ダンパ9,1oがガス流れを阻止している状態を示し、
−点鎖線はバタフライダンパ9,10の移動方向を示す
。The inlet exhaust gas 4 flows vertically through the inlet catalyst section from the top of the catalyst 2 to become the outlet exhaust gas 5. However, the gas passage is divided above the catalyst 2, and the separation of the gas passing through the catalyst (the distance between the catalyst and the catalyst is minimized) A partition plate 11 is arranged so as to minimize leakage of gas into the other divided passage.A butterfly damper 9 is installed in each gas passage formed by the partition plate 11. 10 is supported and installed by the fulcrum 6. In addition, in FIG. 6, the dotted line indicates the state in which the butterfly dampers 9 and 1o are blocking the gas flow.
- The dashed dotted line indicates the moving direction of the butterfly dampers 9, 10.
このような装置において、脱硝装置運転中に、片方はバ
タフライダンパ、例えばバタフライダンパ9、を除々に
ガス流れを阻止するように閉方向に操作し、(必らずし
も全開状態にする必要はない)、他方のガス通路のガス
流速を所要の値まで上げ、ひいては触媒孔内を通過する
ガス流速を上げて、排ガスのマスフローによシ触媒に付
着したダストを搬送除去するようにする。In such a device, while the denitration device is operating, one of the butterfly dampers, such as butterfly damper 9, is operated in the closing direction so as to gradually block the gas flow (it is not necessarily necessary to fully open the butterfly damper). (No), the gas flow rate in the other gas passage is increased to a required value, and the gas flow rate passing through the catalyst holes is increased, so that the dust attached to the catalyst is transported and removed by the mass flow of exhaust gas.
一方の触媒層のダストの除去が終えたならば、バタフラ
イダンパ9を全開状態にもどし、他のバタフライダンパ
10を上記と同様な操作をして他方の触媒層のダストを
除去するようKする。After removing the dust from one catalyst layer, the butterfly damper 9 is returned to the fully open state, and the other butterfly damper 10 is operated in the same manner as described above to remove the dust from the other catalyst layer.
排ガス自身の自浄作用としては排ガス流速を上げること
が、最も手つとり早い方法であり、本発明者のテストに
よシその効果を第5図の通シ確認している。すなわち、
触媒孔内流速を成る速度、例えば11m/秒以上にする
と触媒に付着したダストは排ガスのマスフローにより!
送除去され、流速を上げるにつれてダスト除去所要時間
は減少し効果が大きくなっていくことがわかる。As for the self-cleaning action of the exhaust gas itself, increasing the flow rate of the exhaust gas is the quickest method, and the inventor's tests have confirmed the effect as shown in FIG. 5. That is,
If the flow velocity in the catalyst hole is set to a speed higher than 11 m/sec, for example, dust adhering to the catalyst will be removed by the mass flow of exhaust gas!
It can be seen that as the flow rate increases, the time required for dust removal decreases and the effect increases.
一方、触媒圧力損失は流速を上げるにつれて増大してゆ
き、この値の許容限度は個々のプラントごとの制限値に
左右される。但し、許容限度以内でのある程度の触媒圧
の損失の上昇は短時間(数分以内)であれば許容される
。On the other hand, the catalyst pressure drop increases as the flow rate increases, and the permissible limit of this value depends on the limits for each individual plant. However, a certain increase in catalyst pressure loss within the allowable limit is permissible for a short period of time (within several minutes).
しかし、上述した従来のように構成されたダスト除去装
置には次のような問題がある。However, the conventional dust removal device described above has the following problems.
■ バタフライダンパであるので、触媒と間隔をおいて
設けなくてはならぬので、ガスもれを防ぐため、触媒に
隣接し、かつ、ガス通路を分割する仕切り板が必要不可
欠である。■ Since it is a butterfly damper, it must be installed at a distance from the catalyst, so in order to prevent gas leakage, a partition plate adjacent to the catalyst and dividing the gas passage is essential.
■ バタフライダンパが少なくとも2組以上必要である
■ 上記■、■に示した理由により機構が複雑でコスト
が高くなる。■ At least two or more sets of butterfly dampers are required.■ Due to the reasons shown in (1) and (3) above, the mechanism is complicated and costs are high.
以上の技術水準に鑑み、本発明は構造が簡単で安価にで
きる脱硝装置のダスト除去装置を提供しようとするもの
である。In view of the above state of the art, the present invention aims to provide a dust removal device for a denitrification device that has a simple structure and can be inexpensive.
本発明は多量のダストを含む排ガスを触媒を用いて脱硝
する装置において、触媒充填部に近接して、その上流側
又は下流側に1個または2個以上のヒンジ式ダンパを設
けてなることを特徴とする脱硝装置のダスト除去装置で
ある。The present invention provides an apparatus for denitrating exhaust gas containing a large amount of dust using a catalyst, in which one or more hinged dampers are provided on the upstream or downstream side of the catalyst filling section, in the vicinity of the catalyst filling section. This is a dust removal device for a denitrification device.
ヒンジ式ダンパであるので触媒充填部に近接して設ける
ことができ、そのため、仕切板を設けることが省略でき
、ヒンジ式ダンパを左または右に動かすことによってガ
ス流路を変更し、流通するガス流速を高め、触媒層に付
着したダストの除去が行われる。なお、本発明装置は触
媒として並行流型触媒を用いた時に1特に効果を奏する
。Since it is a hinge type damper, it can be installed close to the catalyst filling part, so it is not necessary to provide a partition plate, and by moving the hinge type damper to the left or right, the gas flow path can be changed and the gas flowing The flow rate is increased to remove dust attached to the catalyst layer. The device of the present invention is particularly effective when a parallel flow type catalyst is used as the catalyst.
本発明でいうヒンジ式ダンパとは支点を中心に水平方向
180°間を移動できるダンパを云う。これに対し、従
来のバタフライダンパは支点を中心に360°間を移動
できるものである。The hinge type damper as used in the present invention refers to a damper that can move horizontally through 180 degrees around a fulcrum. In contrast, a conventional butterfly damper can move through 360 degrees around a fulcrum.
本発明の種々の実施態様を第1図〜第4図によって説明
する。第1図〜第4図において第6図と同一符号は、第
6図と同一のものを意味するので説明は省略する。Various embodiments of the present invention will be explained with reference to FIGS. 1 to 4. In FIGS. 1 to 4, the same reference numerals as in FIG. 6 mean the same parts as in FIG. 6, and therefore the explanation will be omitted.
第1図の実施例において、7は触媒2充填層に近接して
設けられた支点6を中心として動作するヒンジ式ダンパ
で、点線は該ダンパ7の使用状態を示し、−点鎖線は該
ダンパ7の移動方向を示す。In the embodiment shown in FIG. 1, 7 is a hinged damper that operates around a fulcrum 6 provided close to the packed bed of catalyst 2, the dotted line indicates the usage state of the damper 7, and the dashed line indicates the damper. 7 shows the direction of movement.
脱硝装置運転中に該ダンパ7の羽根を交互に操作し触媒
2内を通過するガス流速を上げることKより、触媒の全
域に付着したダストを除去する。During operation of the denitrification device, the blades of the damper 7 are alternately operated to increase the gas flow rate passing through the catalyst 2, thereby removing dust attached to the entire area of the catalyst.
第2図の実施例は第1図におけるヒンジ式ダンパ7の羽
根が使用状態でも片方のガス通路全部をカバーしない場
合を示す。こ−にダンパ7は触媒内通過ガス流速を付着
ダスト除去のための適当値に上げることが目的であシ、
通常運転時の流速がもともと大きい場合はこのようにし
てもよい。The embodiment shown in FIG. 2 shows a case where the blades of the hinge type damper 7 shown in FIG. 1 do not cover the entire gas passage on one side even when in use. The purpose of the damper 7 is to increase the flow rate of gas passing through the catalyst to an appropriate value for removing attached dust.
This may be done if the flow velocity during normal operation is originally high.
第5図の実施例は脱硝反応器1が相対的に大型となシ、
とンジ式ダンパ7及びその駆動機構の小型化のためにヒ
ンジ式ダンパ7を複数配置した場合を示す。In the embodiment shown in FIG. 5, the denitrification reactor 1 is relatively large.
A case is shown in which a plurality of hinge type dampers 7 are arranged in order to downsize the hinge type damper 7 and its drive mechanism.
第4図の実施例は第1図におけるヒンジ式ダンパ7を触
媒2の上流に配置した場合を示す。The embodiment shown in FIG. 4 shows a case where the hinged damper 7 in FIG. 1 is arranged upstream of the catalyst 2.
本発明によシ、ヒンジ式ダンパを触媒充填層に近接して
設けることによシ、構造が簡素化した脱硝装置用ダスト
除去装置が提供できる。According to the present invention, by providing the hinge type damper close to the catalyst packed bed, it is possible to provide a dust removal device for a denitrification device with a simplified structure.
第1図〜第4図は発明の実施例を示す概略図、第5図は
触媒孔内ガス流速(m/秒)と付着ダスト完全除去所要
時間(秒)及び触媒圧の損失(mAq )の関係を示す
図表、第6図は従来の脱硝装置のダスト除去装置の一態
様を示す概略図である。Figures 1 to 4 are schematic diagrams showing embodiments of the invention, and Figure 5 shows the relationship between the gas flow rate in the catalyst hole (m/sec), the time required for complete removal of attached dust (sec), and the catalyst pressure loss (mAq). FIG. 6, a chart showing the relationship, is a schematic diagram showing one aspect of a conventional dust removal device of a denitrification device.
Claims (1)
において、触媒充填部に近接して、その上流側又は下流
側に1個または2個以上のヒンジ式ダンパを設けてなる
ことを特徴とする脱硝装置のダスト除去装置。An apparatus for denitrating exhaust gas containing a large amount of dust using a catalyst, characterized in that one or more hinged dampers are provided close to the catalyst filling part and on the upstream or downstream side thereof. Dust removal device for denitrification equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63173951A JPH0829222B2 (en) | 1988-07-14 | 1988-07-14 | Dust removal equipment for denitration equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63173951A JPH0829222B2 (en) | 1988-07-14 | 1988-07-14 | Dust removal equipment for denitration equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0226620A true JPH0226620A (en) | 1990-01-29 |
JPH0829222B2 JPH0829222B2 (en) | 1996-03-27 |
Family
ID=15970083
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63173951A Expired - Lifetime JPH0829222B2 (en) | 1988-07-14 | 1988-07-14 | Dust removal equipment for denitration equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0829222B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007061667A (en) * | 2005-08-29 | 2007-03-15 | Hitachi Zosen Corp | Flow velocity control device in high-dust denitration reactor |
WO2014178337A1 (en) * | 2013-05-01 | 2014-11-06 | 東京博善株式会社 | Cremation system and cremation method |
CN106996572A (en) * | 2017-03-21 | 2017-08-01 | 华电电力科学研究院 | Solve the flue gas recirculation structure and method of SCR denitration underrun dust stratification abrasion |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5326263A (en) * | 1976-08-24 | 1978-03-10 | Kobe Steel Ltd | Denitrating apparatus for exhaust gas |
JPS5658525A (en) * | 1979-10-19 | 1981-05-21 | Hitachi Ltd | Removing method of adhered dust of platelike catalyst |
JPS60119921U (en) * | 1984-01-23 | 1985-08-13 | 石川島播磨重工業株式会社 | Dust removal equipment for denitrification reactor |
-
1988
- 1988-07-14 JP JP63173951A patent/JPH0829222B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5326263A (en) * | 1976-08-24 | 1978-03-10 | Kobe Steel Ltd | Denitrating apparatus for exhaust gas |
JPS5658525A (en) * | 1979-10-19 | 1981-05-21 | Hitachi Ltd | Removing method of adhered dust of platelike catalyst |
JPS60119921U (en) * | 1984-01-23 | 1985-08-13 | 石川島播磨重工業株式会社 | Dust removal equipment for denitrification reactor |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007061667A (en) * | 2005-08-29 | 2007-03-15 | Hitachi Zosen Corp | Flow velocity control device in high-dust denitration reactor |
JP4565281B2 (en) * | 2005-08-29 | 2010-10-20 | 日立造船株式会社 | High dust denitration reactor |
WO2014178337A1 (en) * | 2013-05-01 | 2014-11-06 | 東京博善株式会社 | Cremation system and cremation method |
JP5721914B2 (en) * | 2013-05-01 | 2015-05-20 | 東京博善株式会社 | Cremation system and cremation method |
CN106996572A (en) * | 2017-03-21 | 2017-08-01 | 华电电力科学研究院 | Solve the flue gas recirculation structure and method of SCR denitration underrun dust stratification abrasion |
Also Published As
Publication number | Publication date |
---|---|
JPH0829222B2 (en) | 1996-03-27 |
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