JP2739439B2 - Wet desulfurization equipment - Google Patents

Wet desulfurization equipment

Info

Publication number
JP2739439B2
JP2739439B2 JP6270207A JP27020794A JP2739439B2 JP 2739439 B2 JP2739439 B2 JP 2739439B2 JP 6270207 A JP6270207 A JP 6270207A JP 27020794 A JP27020794 A JP 27020794A JP 2739439 B2 JP2739439 B2 JP 2739439B2
Authority
JP
Japan
Prior art keywords
gas
desulfurizer
chamber
processing
vortex
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
JP6270207A
Other languages
Japanese (ja)
Other versions
JPH08108036A (en
Inventor
誠一 和田
一宏 赤池
武俊 安宗
めぐみ 田口
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 Kakoki Kaisha Ltd
Japan Petroleum Energy Center JPEC
Original Assignee
Petroleum Energy Center PEC
Mitsubishi Kakoki Kaisha Ltd
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 Petroleum Energy Center PEC, Mitsubishi Kakoki Kaisha Ltd filed Critical Petroleum Energy Center PEC
Priority to JP6270207A priority Critical patent/JP2739439B2/en
Publication of JPH08108036A publication Critical patent/JPH08108036A/en
Application granted granted Critical
Publication of JP2739439B2 publication Critical patent/JP2739439B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Chimneys And Flues (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation Of Particles Using Liquids (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、化石燃料を使用するボ
イラ、陸上および舶用ディーゼルエンジンの排ガス中に
含まれるダストおよびイオウ酸化物などを同時に除去す
る湿式脱硫装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wet desulfurization apparatus for simultaneously removing dust and sulfur oxides contained in exhaust gas from boilers using fossil fuels, land and marine diesel engines.

【0002】[0002]

【従来の技術】化石燃料を使用するボイラや、陸上およ
び舶用ディーゼルエンジンの排ガス中には、比較的多量
のダストやイオウ酸化物が含まれており、それを大気中
に排気することで公害問題になっている。そこで、これ
を解消するものとして、各種の脱硫装置が開発されてい
る。
2. Description of the Related Art Exhaust gas from boilers using fossil fuels and onshore and marine diesel engines contains a relatively large amount of dust and sulfur oxides. It has become. Therefore, various desulfurization apparatuses have been developed to solve this problem.

【0003】従来の湿式脱硫装置として、例えば特公昭
43−3280号公報に記載されたものなどが知られて
いる。この装置は、一方の側にガス流の導入口を有する
1つの分離容器と、この分離容器内に入れた液と、分離
容器の他方の側に接続されたポンプと、上記の導入口の
付近において分離容器内に設けられ気流を液面に対して
ほぼ直角に指向させる外らせ板と、その前方かつ上方に
設けられ内方に開口している円筒状の室と、前述したほ
ぼ直角方向気流の影響により、前流側と後流側とにおい
て液面のレベル差を形成させるようにした傾斜配置の壁
部材と分離容器の壁とにより、液面のところから斜め上
方に指向して形成された気流通路とを備えたものであ
る。
[0003] As a conventional wet desulfurization apparatus, for example, one described in Japanese Patent Publication No. 43-3280 is known. The apparatus comprises a separation vessel having a gas flow inlet on one side, a liquid contained in the separation vessel, a pump connected to the other side of the separation vessel, and a vicinity of the inlet. A deflector plate provided in the separation vessel for directing the air flow substantially at right angles to the liquid surface, a cylindrical chamber provided in front of and above and open inward, and the above-described substantially right-angled direction. Formed obliquely upward from the liquid level by the wall of the inclined container and the wall of the separation vessel, which form a level difference between the liquid level on the upstream side and the downstream side due to the influence of the air flow. And an airflow passage.

【0004】ガス流の導入口から導入された処理ガス
は、ブロアの駆動による負圧力がかかると、外らせ板を
介して分離容器内に貯留された液面にほぼ直角に潜り込
んで、処理ガス中のダストが液中に沈澱したりして除去
される一方、ガス部分は主に円筒状の室内で渦流になっ
て液分と接触されて脱硫され、その後、上方傾斜した気
流通路に沿って上昇して処理済ガスが排出されるもので
ある。
When a negative pressure is applied by driving a blower, the processing gas introduced from the gas flow inlet enters the liquid level stored in the separation container through a deflector plate at a substantially right angle, and the processing gas is processed. While the dust in the gas precipitates and is removed in the liquid, the gas part is swirled mainly in the cylindrical chamber and is brought into contact with the liquid to be desulfurized, and then along the upwardly inclined air passage. And the treated gas is discharged.

【0005】[0005]

【発明が解決しようとする課題】ところで、従来の湿式
脱硫装置では、ボイラやエンジンの出力増大に伴って処
理ガス量が増加する場合、分離容器を、縦、横、高さの
全体的に大型化して対応させていたが、この方法を採用
した場合、処理ガス量の増加度合いによっては、スペー
ス的に排ガスの煙道設置が不可能となり、排ガスダクト
をその回避方向へ引き回すことになっていた。
By the way, in the conventional wet desulfurization apparatus, when the processing gas amount increases with the increase in the output of the boiler or the engine, the separation vessel is required to be large in length, width and height. However, if this method was adopted, depending on the degree of increase in the amount of gas to be treated, it would not be possible to install exhaust gas flue in space, and the exhaust gas duct would be routed in the direction to avoid it. .

【0006】これにより、この脱硫装置を設置する際に
は、予め処理ガス量の増加時の対策をも見越して、広い
設置スペースが必要であるという問題点があった。ま
た、処理ガス量が増加すると、前記外らせ板の下端と分
離容器との隙間を通過するガス通過流速が大きくなり、
圧力損失を増大させるという問題点があった。
Accordingly, when this desulfurization apparatus is installed, there is a problem that a large installation space is required in anticipation of a countermeasure when the amount of processing gas is increased in advance. Further, when the amount of the processing gas increases, the gas flow velocity passing through the gap between the lower end of the deflector and the separation container increases,
There was a problem of increasing the pressure loss.

【0007】本発明は、前記従来技術の課題を背景にな
されたもので、処理ガス量が増加しても、煙道周辺の設
置規制の有無に係わりなく煙道設置が可能であり、しか
も圧力損失も安定している湿式脱硫装置を提供すること
を目的とする。
[0007] The present invention has been made in view of the above-mentioned problems of the prior art. Even if the amount of treated gas is increased, the flue can be installed regardless of whether or not the installation around the flue is regulated. It is an object of the present invention to provide a wet desulfurization device having stable loss.

【0008】[0008]

【課題を解決するための手段】本発明は、脱硫器の容器
内が、処理ガスのガス入口と、ガス吹き出し口が形成さ
れたガス導入室と、該ガス導入室内に脱硫処理液の噴射
ノズルが設けられた前記ガス導入室のガス吹き出し口に
連通して、上流側の上部にほぼ円筒状の渦流発生部が設
けられ、下流側に上傾斜通路部が設けられた渦流処理室
と、該渦流処理室の上傾斜通路部に連通されて、上部に
処理済ガスのガス出口が形成されたガス排出室とに仕切
られ、前記脱硫器を、前記処理ガスの煙道方向に沿って
複数台並設させ、全ての前記脱硫器のガス入口に連通す
一つのガス導入部を設けるとともに、全ての前記脱硫
器のガス出口に連通する一つのガス排出部を設けたこと
を特徴とする湿式脱硫装置を提供するものである。
SUMMARY OF THE INVENTION The present invention is directed to a desulfurizer vessel.
Inside is a gas inlet for the processing gas, a gas introduction chamber having a gas outlet, and injection of a desulfurization treatment liquid into the gas introduction chamber.
A vortex processing chamber provided with a substantially cylindrical vortex generator at the upper part on the upstream side and an upper inclined passage part on the downstream side, communicating with a gas outlet of the gas introduction chamber provided with a nozzle ; The vortex processing chamber communicates with the upper inclined passage portion and is partitioned into a gas discharge chamber in which a gas outlet of the processed gas is formed at an upper portion, and the desulfurizer is provided in a plurality along the flue direction of the processing gas. A wet type, in which a plurality of tables are arranged side by side, and one gas introduction part communicating with the gas inlets of all the desulfurizers is provided, and one gas discharge part communicating with the gas outlets of all the desulfurizers is provided. A desulfurization device is provided.

【0009】[0009]

【作用】本発明の湿式脱硫装置において、処理ガスは
ての前記脱硫器のガス入口に連通する一つのガス導入部
を介して、煙道方向に沿って並設されたそれぞれの脱硫
器のガス入口から各容器のガス導入室を通過し、この途
中でガス導入室に設けられた噴射ノズルから噴射される
脱硫処理液に接触することにより吸収され、次いでガス
導入室の下部のガス吹き出し口から渦流処理室内へ吹き
出された処理ガスおよび霧状の脱硫処理液は渦流発生部
内で渦流となり、遠心力によりその渦流発生部の形成面
に当たって液膜ができ、処理ガス中のダストは液膜に補
集されて、容器の底部に貯溜される。その後、ほとんど
処理が済んだ処理ガスと幾らかの霧状の脱硫処理液は、
渦流処理室の上傾斜通路部の形成面にも液膜を作って脱
硫およびダストの補集が行われる。そして、上傾斜通路
部からガス排出室へ送られた処理済ガスは、そこに形成
されたガス出口より、各脱硫器のガス出口の全てに連通
された一つのガス排出部へ一括して流れ込み、それを通
して外部排出される。
In the wet desulfurization apparatus of the present invention, the processing gas is entirely
Through one gas inlet communicating with the gas inlets of all of the above desulfurizers, the gas passes through the gas inlet chamber of each container from the gas inlets of the respective desulfurizers juxtaposed along the flue direction. Is injected from the injection nozzle provided in the gas introduction chamber
The processing gas and the mist-like desulfurization processing liquid that are absorbed by contacting the desulfurization processing liquid and then blown into the vortex processing chamber from the gas outlet at the lower part of the gas introduction chamber become vortex in the vortex generation part, and the centrifugal force causes the vortex. A liquid film is formed on the surface on which the vortex flow generating section is formed, and dust in the processing gas is collected by the liquid film and stored at the bottom of the container. After that, the treated gas and some mist-like desulfurization treatment liquid,
A liquid film is also formed on the upper inclined passage portion forming surface of the vortex processing chamber to perform desulfurization and dust collection. The processed gas sent from the upper inclined passage to the gas discharge chamber collectively flows from the gas outlet formed there into one gas discharge part connected to all of the gas outlets of each desulfurizer. , Through which it is discharged outside.

【0010】煙道を流れる処理ガス量が増加した場合に
は、煙道方向に沿って並設される脱硫器の個数を増加さ
せると、煙道周辺の設置規制の有無に係わりなく煙道設
置が可能であり、しかも処理ガスの圧力損失に影響が大
きい円筒状の渦流発生部が、従来のように処理ガス量の
増加に対応させても大型化しないので、湿式脱硫装置内
での圧力損失も安定している。
When the amount of processing gas flowing through the flue increases, the number of desulfurizers juxtaposed along the flue direction can be increased, regardless of whether or not there are restrictions on the installation around the flue. In addition, the cylindrical vortex generator, which has a large effect on the pressure loss of the processing gas, does not become large even if the processing gas volume is increased as in the past. Is also stable.

【0011】さらに本発明の湿式脱硫装置において、
各容器内へ導入された処理ガスは、上記のごとく、ガス
導入室を通過中に噴射ノズルから脱硫処理液が噴射され
る。この際、それぞれの噴射ノズルからの脱硫処理液の
噴出量を各脱硫器毎に増減させて、ちょうど弁のように
処理ガスの流入抵抗を調整することにより、脱硫器が煙
道方向に沿って横長に並設されていることを原因とした
ガス導入部から各脱硫器へ分配される処理ガスの偏流発
生などを防止して、均等な処理ガスの分配を実現でき
る。
Further , in the wet desulfurization apparatus of the present invention ,
As described above, the desulfurization treatment liquid is injected from the injection nozzle while the processing gas introduced into each container passes through the gas introduction chamber. At this time, by increasing or decreasing the amount of the desulfurization treatment liquid ejected from each injection nozzle for each desulfurizer, and adjusting the inflow resistance of the treatment gas just like a valve, the desulfurizer is moved along the flue direction. The occurrence of uneven flow of the processing gas distributed from the gas inlet to the respective desulfurizers due to the horizontally-arranged arrangement can be prevented, and uniform processing gas distribution can be realized.

【0012】[0012]

【実施例】以下、本発明の実施例を図面を参照して詳細
に説明するが、本発明はこの実施例に限定されない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings, but the present invention is not limited to these embodiments.

【0013】まず、図1〜3に基づいて、本発明の第1
実施例の湿式脱硫装置を説明する。図1〜2に示すよう
に、本発明の第1実施例の湿式脱硫装置10は、脱硫器
20を、処理ガスの煙道方向に沿って6台並設させ、全
ての脱硫器20のガス入口21に連通する一つのガス導
入部22を設けるとともに、全ての脱硫器20のガス出
口23に連通する一つのガス排出部24を設けたもので
ある。なお、ガス導入部22とガス排出部24とは一体
化したボックス状となっており、ガス導入部22にはダ
ストの上流側に接続されるガス導入口22aが設けら
れ、ガス排出部24にはダストの下流側に接続されるガ
ス排出口24aが設けられている。
First, a first embodiment of the present invention will be described with reference to FIGS.
A wet desulfurization apparatus according to an embodiment will be described. As shown in FIGS. 1 and 2, in the wet desulfurization apparatus 10 of the first embodiment of the present invention, six desulfurizers 20 are juxtaposed along the flue direction of the processing gas. One gas inlet 22 communicating with the inlet 21 is provided, and one gas outlet 24 communicating with the gas outlets 23 of all the desulfurizers 20 is provided. The gas inlet 22 and the gas outlet 24 are in the form of an integrated box. The gas inlet 22 is provided with a gas inlet 22a connected to the upstream side of the dust. Is provided with a gas outlet 24a connected to the downstream side of the dust.

【0014】図3に示すように、脱硫器20は、煙道方
向に直交する方向へ横長な容器30を有しており、容器
30のガス入口21側の端部が、垂直板31により仕切
られて、高さ方向の中間部付近に脱硫処理液aの噴射ノ
ズル32が設けられたガス導入室33となっている。脱
硫処理液aとして、例えば石灰石や消石灰などの吸収剤
と吸収生成物である石膏や亜硫酸カルシウムなどとの混
合物からなるスラリー状のものや、酸化マグネシウムや
亜硫酸マグネシウムなどの吸収剤と吸収生成物である硫
酸マグネシウムや亜硫酸マグネシウムなどの混合物から
なる溶液またはスラリー状のものなどを採用することが
好ましいが、その他のアルカリ塩溶液なも採用できる。
As shown in FIG. 3, the desulfurizer 20 has a container 30 which is long in the direction perpendicular to the flue direction, and the end of the container 30 on the gas inlet 21 side is partitioned by a vertical plate 31. The gas introduction chamber 33 is provided with an injection nozzle 32 for the desulfurization treatment liquid a near an intermediate portion in the height direction. As the desulfurization treatment liquid a, for example, a slurry made of a mixture of an absorbent such as limestone or slaked lime and an absorption product such as gypsum or calcium sulfite, or an absorbent and an absorption product such as magnesium oxide or magnesium sulfite. It is preferable to use a solution or slurry made of a mixture of certain magnesium sulfate and magnesium sulfite, but other alkali salt solutions can also be used.

【0015】ガス導入室33の下部には、ガス吹き出し
口34が形成されており、ガス導入室33の下流に、ガ
ス吹き出し口34に連通して渦流処理室35が形成され
ている。渦流処理室35は、上流側の上部に配置され
て、一端が垂直板31の中間部に固着され、かつ下面が
開口された湾曲板36により区画されたほぼ円筒状の渦
流発生部37と、湾曲板36の内方へ捲くり込まれた他
端から立ち上がって、一旦、容器30の中央上端まで延
びたのち、円弧状に下降してガス出口23付近に取り付
けられたフィルタ38の装着部に取り付けられた上側通
路板39および下流側に配置されて、下端が容器30の
底部から上側通路板39に沿って立ち上がった下側通路
板40により区画された上傾斜通路部41とにより構成
されている。
A gas outlet 34 is formed below the gas introduction chamber 33, and a vortex processing chamber 35 is formed downstream of the gas introduction chamber 33 so as to communicate with the gas outlet 34. The eddy current processing chamber 35 is disposed at an upper portion on the upstream side, has one end fixed to an intermediate portion of the vertical plate 31, and has a substantially cylindrical eddy current generating portion 37 defined by a curved plate 36 having an open lower surface. It rises from the other end that is rolled inward of the curved plate 36, once extends to the upper end of the center of the container 30, and then descends in an arc shape to the mounting portion of the filter 38 attached near the gas outlet 23. An upper inclined passage portion 41 is provided, which is disposed on the downstream side of the upper passage plate 39 attached thereto and has a lower end defined by a lower passage plate 40 rising from the bottom of the container 30 along the upper passage plate 39. I have.

【0016】この渦流処理室35の下流には、上傾斜通
路部41に連通されて、上部に前記処理済ガスのガス出
口23が形成されたガス排出室42が配置されており、
また容器30の底部には、ガス入口21側の端部からガ
ス出口23側の端部へ徐々に下方傾斜するドレン部43
が設けられており、ドレン部43の最下端部に、排出管
44に接続された脱硫処理後の廃液の排出口45が形成
されている。
Downstream of the vortex processing chamber 35, there is disposed a gas discharge chamber 42 communicating with the upper inclined passage 41 and having the gas outlet 23 for the processed gas formed at the upper part thereof.
At the bottom of the container 30, a drain portion 43 that is gradually inclined downward from an end on the gas inlet 21 side to an end on the gas outlet 23 side is provided.
Is provided at the lowermost end of the drain portion 43, and a discharge port 45 for the waste liquid after the desulfurization treatment connected to the discharge pipe 44 is formed.

【0017】次に、本発明の第1実施例の湿式脱硫装置
10の動作を説明する。図1〜2に示すように、イオウ
酸化物やダストを含んだ処理ガスを、図外のダクトを介
してガス導入口22aから湿式脱硫装置10内へ導入さ
せると、まず処理ガスは一つのガス導入部22を直進し
て、煙道方向に沿って並設されたそれぞれの脱硫器20
のガス入口21から各容器20のガス導入室33へ導か
れ、ここで噴射ノズル32から脱硫処理液aが噴射され
て、処理済ガス中のイオウ酸化物が吸収される。
Next, the operation of the wet desulfurization apparatus 10 according to the first embodiment of the present invention will be described. As shown in FIGS. 1 and 2, when a processing gas containing sulfur oxides and dust is introduced into the wet desulfurization apparatus 10 from a gas inlet 22 a through a duct (not shown), first, one processing gas is formed. The desulfurizers 20 are arranged in a straight line along the flue direction through the introduction section 22.
From the gas inlet 21 to the gas introduction chamber 33 of each container 20, where the desulfurization treatment liquid a is injected from the injection nozzle 32 to absorb the sulfur oxides in the processed gas.

【0018】この際、脱硫器20が煙道方向に沿って横
長に並設されているので、一つの長尺なガス導入部22
から各脱硫器20へ分配される途中の処理ガスに偏流が
発生して均等なガス配分ができなくなる恐れがあるが、
そのような場合には、それぞれの噴射ノズル32からの
脱硫処理液aの噴出量を各脱硫器20毎に増減させて、
ちょうど弁のように処理ガスの流入抵抗を調整すること
により、この均等な処理ガスの分配が実現できる。
At this time, since the desulfurizers 20 are arranged horizontally long in the flue direction, one long gas introduction portion 22 is provided.
However, there is a risk that uneven flow may occur in the processing gas being distributed to the respective desulfurizers 20 and the gas may not be distributed evenly.
In such a case, the ejection amount of the desulfurization treatment liquid a from each injection nozzle 32 is increased or decreased for each desulfurizer 20.
By adjusting the inflow resistance of the processing gas just like a valve, this uniform distribution of the processing gas can be realized.

【0019】次いで、ガス導入室33のガス吹き出し口
34において、10m/s以上に加速された処理済ガス
や霧状の脱硫処理液aは渦流処理室35内へ吹き出さ
れ、ここの渦流発生部37内で渦流となり、遠心力によ
りその渦流発生部37の形成面である湾曲板36の内面
に当たって液膜ができ、処理ガス中のダストは液膜に補
集されて、容器20の底部のドレン部43へ流れ落ち
る。
Next, at the gas outlet 34 of the gas introduction chamber 33, the processed gas and the mist-like desulfurization processing liquid a accelerated to 10 m / s or more are blown out into the vortex processing chamber 35, where the vortex generator A vortex is formed in the vortex 37, and a liquid film is formed by the centrifugal force on the inner surface of the curved plate 36 on which the vortex flow generating portion 37 is formed. Dust in the processing gas is collected by the liquid film, and the drain at the bottom of the container 20 is drained. It flows down to the part 43.

【0020】その後、ほとんど処理が済んだ処理ガスと
幾らかの霧状の脱硫処理液aは、上傾斜通路部41の形
成面である上下側通路板39、40の内面にも液膜を作
って脱硫およびダストの補集が行われる。そして、上傾
斜通路部41を通過してガス排出室42へ送られた処理
済ガスは、フィルタ38により液分などがろ過されてガ
ス出口23より、各脱硫器20の全てに連通された一つ
ガス排出部24へ一括して流れ込み、ダクトを介して
外部排出される。また、ダストを含む脱硫処理後の廃液
は、ドレン部43により集められて排出口45から排出
管44を通して排出される。
Thereafter, the treated gas and the desulfurized treatment liquid a in the form of some mist form a liquid film also on the inner surfaces of the upper and lower passage plates 39 and 40 on which the upper inclined passage portion 41 is formed. Desulfurization and dust collection. Then, the treated gas delivered through on the inclined passage 41 into the gas discharge chamber 42, such as liquid component is filtered by a filter 38 and the gas outlet 23, which communicates with all of the desulfurizer 20 one One
, And collectively flows into the gas discharge part 24 and is discharged outside through a duct. Further, the waste liquid containing the dust after the desulfurization treatment is collected by the drain part 43 and discharged from the discharge port 45 through the discharge pipe 44.

【0021】煙道を流れる処理ガス量が増加した場合に
は、煙道方向に沿って並設される脱硫器20の個数を増
加させればよく、これにより煙道周辺の設置規制の有無
に係わりなく煙道設置が可能であり、しかも処理ガスの
圧力損失に影響が大きい円筒状の渦流発生部37が、従
来のように処理ガス量の増加に対応させても大型化しな
いので、湿式脱硫装置10内での圧力損失も安定化でき
る。
When the amount of the processing gas flowing through the flue increases, the number of desulfurizers 20 juxtaposed along the flue direction may be increased. Irrespective of this, the flue can be installed, and the cylindrical vortex generator 37, which has a large influence on the pressure loss of the processing gas, does not become large even if the processing gas volume is increased as in the prior art. The pressure loss in the device 10 can also be stabilized.

【0022】次に、図4に基づいて、本発明の第2実施
例の湿式脱硫装置50を説明する。図4に示すように、
本発明の第2実施例の湿式脱硫装置50は、脱硫器20
を煙道方向に対して斜めに並設接続させ、また一つの
ス導入部51と一つのガス排出部52をそれぞれ先細り
と先太りの通路としたものである。このようにすること
で、各脱硫器20への処理ガスの均等分配が実現でき、
またガス導入部51とガス排出部52の容積を小さくで
きるため、全体としてコンパクトな装置になるという効
果が得られる。
Next, a wet desulfurization apparatus 50 according to a second embodiment of the present invention will be described with reference to FIG. As shown in FIG.
The wet desulfurization apparatus 50 according to the second embodiment of the present invention includes a desulfurizer 20.
Was juxtaposed connected obliquely to the flue direction, it is one of the gas <br/> scan introducing portion 51 and one gas outlet 52 which was tapered and thickens the passage respectively. By doing so, the processing gas can be evenly distributed to each desulfurizer 20,
Further, since the volumes of the gas introduction part 51 and the gas discharge part 52 can be reduced, an effect that the apparatus becomes compact as a whole can be obtained.

【0023】以上、本発明の実施例を説明したが、本発
明はこの実施例に限定されるものではなく、要旨を逸脱
しない範囲での設計変更などがあっても本発明に含まれ
る。例えば、脱硫器のガス導入室、渦流処理室およびガ
ス排出室の形状は、実施例のものに限定されなくてもよ
い。
Although the embodiment of the present invention has been described above, the present invention is not limited to this embodiment, and any change in design without departing from the scope of the present invention is included in the present invention. For example, the shapes of the gas introduction chamber, the vortex processing chamber, and the gas discharge chamber of the desulfurizer need not be limited to those in the embodiment.

【0024】また、処理ガスの煙道方向に沿って並設さ
れる脱硫器の個数も任意個数でよい
The number of desulfurizers juxtaposed along the flue direction of the processing gas may be any number .

【0025】[0025]

【発明の効果】本発明の湿式脱硫装置は、このように複
数台の脱硫器を、処理ガスの煙道方向に沿って並設さ
せ、全ての脱硫器のガス入口に連通する一つのガス導入
部を設けるとともに、全ての脱硫器のガス出口に連通す
一つのガス排出部を設けるのようにしたので、煙道を
流れる処理ガス量が増加した場合には、煙道方向に沿っ
て並設される脱硫器の個数を増加させればよく、煙道周
辺の設置規制の有無に係わりなく煙道設置が可能であ
り、しかも処理ガスの圧力損失に影響が大きい円筒状の
渦流発生部が、従来のように処理ガス量の増加に対応さ
せても大型化しないので、湿式脱硫装置内での圧力損失
も安定化できる。
Wet flue gas desulfurization apparatus of the present invention exhibits, thus a plurality of the desulfurizer, is arranged along the flue direction of the process gas, a gas inlet communicating with the gas inlet of all the desulfurizer And a single gas discharge unit that communicates with the gas outlets of all desulfurizers, so if the amount of treated gas flowing through the flue increases, it will be juxtaposed along the flue direction. It is only necessary to increase the number of desulfurizers to be installed, and it is possible to install the flue regardless of the installation regulations around the flue, and the cylindrical vortex generator, which has a large effect on the pressure loss of the processing gas, Since the size does not increase even if the amount of processing gas is increased as in the related art, the pressure loss in the wet desulfurization device can be stabilized.

【0026】また、本発明の湿式脱硫装置においては、
ガス導入室内に脱硫処理液の噴射ノズルを設け、それぞ
れの噴射ノズルからの脱硫処理液の噴出量を各脱硫器毎
に増減させて処理ガスの流入抵抗を調整するようにした
ので、脱硫器が煙道方向に沿って横長に並設されている
ことを原因とした一つのガス導入部から各脱硫器へ分配
される処理ガスの偏流発生などを防止して、均等な処理
ガスの分配を実現できる。
Further, in the wet desulfurization apparatus of the present invention ,
A desulfurization treatment liquid injection nozzle is provided in the gas introduction chamber, and the amount of desulfurization treatment liquid ejected from each injection nozzle is increased or decreased for each desulfurizer to adjust the inflow resistance of the processing gas. Prevents uneven flow of processing gas distributed from one gas inlet to each desulfurizer due to the horizontal arrangement along the flue direction, realizing even distribution of processing gas it can.

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

【図1】本発明の第1実施例の湿式脱硫装置の分解斜視
図である。
FIG. 1 is an exploded perspective view of a wet desulfurization apparatus according to a first embodiment of the present invention.

【図2】第1実施例の湿式脱硫装置の斜視図である。FIG. 2 is a perspective view of the wet desulfurization apparatus of the first embodiment.

【図3】第1実施例の要部拡大断面図である。FIG. 3 is an enlarged sectional view of a main part of the first embodiment.

【図4】本発明の第2実施例の湿式脱硫装置の斜視図で
ある。
FIG. 4 is a perspective view of a wet desulfurization apparatus according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 湿式脱硫装置 20 脱硫器 21 ガス入口 22 ガス導入部 23 ガス出口 24 ガス排出部 30 容器 32 噴射ノズル 33 ガス導入室 34 ガス吹き出し口 35 渦流処理室 37 渦流発生部 41 上傾斜通路部 42 ガス排出室 a 脱硫処理液 DESCRIPTION OF SYMBOLS 10 Wet desulfurization apparatus 20 Desulfurizer 21 Gas inlet 22 Gas inlet 23 Gas outlet 24 Gas outlet 30 Vessel 32 Injection nozzle 33 Gas introduction chamber 34 Gas outlet 35 Swirl processing chamber 37 Swirl generator 41 Upper inclined passage part 42 Gas discharge Chamber a Desulfurization treatment liquid

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B01D 53/77 F23J 15/00 B F23J 15/00 (72)発明者 安宗 武俊 神奈川県川崎市川崎区大川町2番1号 三菱化工機株式会社内 (72)発明者 田口 めぐみ 神奈川県川崎市川崎区大川町2番1号 三菱化工機株式会社内 (56)参考文献 特開 平2−99117(JP,A) 特公 昭43−3280(JP,B1)──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI B01D 53/77 F23J 15/00 B F23J 15/00 (72) Inventor Taketoshi Yasune 2-1 Okawa-cho, Kawasaki-ku, Kawasaki-ku, Kawasaki-shi, Kanagawa No. Mitsubishi Koki Co., Ltd. (72) Inventor Megumi Taguchi 2-1 Okawa-cho, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture Mitsubishi Kakoki Co., Ltd. (56) References JP-A-2-99117 (JP, A) Showa 43-3280 (JP, B1)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 脱硫器の容器内が、処理ガスのガス入口
と、ガス吹き出し口が形成されたガス導入室と、該ガス
導入室内に脱硫処理液の噴射ノズルが設けられた前記
ス導入室のガス吹き出し口に連通して、上流側の上部に
ほぼ円筒状の渦流発生部が設けられ、下流側に上傾斜通
路部が設けられた渦流処理室と、該渦流処理室の上傾斜
通路部に連通されて、上部に処理済ガスのガス出口が形
成されたガス排出室とに仕切られ、前記脱硫器を、前記
処理ガスの煙道方向に沿って複数台並設させ、全ての前
記脱硫器のガス入口に連通する一つのガス導入部を設け
るとともに、全ての前記脱硫器のガス出口に連通する
つのガス排出部を設けたことを特徴とする湿式脱硫装
置。
1. A desulfurizer vessel, a gas inlet for the process gas, a gas introduction chamber gas outlet is formed, the gas
An almost cylindrical vortex generator is provided at the upper part on the upstream side, and is connected to the gas outlet of the gas introduction chamber provided with the injection nozzle for the desulfurization treatment liquid in the introduction chamber. The desulfurizer is divided into a vortex processing chamber provided with an upper inclined passage portion, and a gas discharge chamber communicated with the upper inclined passage portion of the vortex processing chamber and formed with a gas outlet for processed gas at an upper portion thereof. It was allowed to plurality Tainami set along the flue direction of the process gas, provided with a single gas inlet communicating with the gas inlet of any of the desulfurizer, communicating with the gas outlet of all the desulfurizer one
A wet desulfurization device comprising two gas discharge units.
JP6270207A 1994-10-11 1994-10-11 Wet desulfurization equipment Expired - Lifetime JP2739439B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6270207A JP2739439B2 (en) 1994-10-11 1994-10-11 Wet desulfurization equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6270207A JP2739439B2 (en) 1994-10-11 1994-10-11 Wet desulfurization equipment

Publications (2)

Publication Number Publication Date
JPH08108036A JPH08108036A (en) 1996-04-30
JP2739439B2 true JP2739439B2 (en) 1998-04-15

Family

ID=17483029

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6270207A Expired - Lifetime JP2739439B2 (en) 1994-10-11 1994-10-11 Wet desulfurization equipment

Country Status (1)

Country Link
JP (1) JP2739439B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0299117A (en) * 1988-10-06 1990-04-11 Agency Of Ind Science & Technol Gas deodorizing apparatus

Also Published As

Publication number Publication date
JPH08108036A (en) 1996-04-30

Similar Documents

Publication Publication Date Title
US4273750A (en) Flue gas desulfurization apparatus and method
US4204847A (en) Mist eliminator device for a wet scrubber apparatus
WO2007116714A1 (en) Wet-type exhaust gas desulfurizer
JPH02290218A (en) Gas absorption tower
EP0640373B1 (en) Spray tower and method for cooling, moistening and/or purifying gas
JP3073972B2 (en) Flue gas desulfurization equipment
CA2006246A1 (en) Scrubbing column for an apparatus for the desulfurization of flue gases
JP2739439B2 (en) Wet desulfurization equipment
JP3861047B2 (en) Exhaust gas purifier
JP3322455B2 (en) Water spray type air purification device
JP3565943B2 (en) Wet desulfurization equipment
JP2003103139A (en) Wet process flue gas desulfurizer
JP3319631B2 (en) Water spray type air purification device
KR102069593B1 (en) Absorption tower of flue gas desulfurizer
JPH10192646A (en) Horizontal flow and wet type flue gas desulfurization device with mist removing function
JP3322456B2 (en) Water spray type air purification device
JP3517298B2 (en) Flue gas desulfurization equipment
JPH07229325A (en) Desulfurization stack
CN213492711U (en) White-removing and demisting device and spray tower
SU1613143A1 (en) Apparatus for wet cleaning of gas
JP2001149746A (en) Absorption tower of desulfurizing device
JPH08196864A (en) Wet desulfurization of waste gas and device therefor
RU195515U1 (en) Wet gas purifier
JPH06154550A (en) Absorption device
RU2115461C1 (en) Gas treatment apparatus

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19971209

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080123

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090123

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100123

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100123

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110123

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120123

Year of fee payment: 14

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130123

Year of fee payment: 15

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130123

Year of fee payment: 15

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140123

Year of fee payment: 16

EXPY Cancellation because of completion of term