JP2549604Y2 - Exhaust gas treatment equipment - Google Patents

Exhaust gas treatment equipment

Info

Publication number
JP2549604Y2
JP2549604Y2 JP536292U JP536292U JP2549604Y2 JP 2549604 Y2 JP2549604 Y2 JP 2549604Y2 JP 536292 U JP536292 U JP 536292U JP 536292 U JP536292 U JP 536292U JP 2549604 Y2 JP2549604 Y2 JP 2549604Y2
Authority
JP
Japan
Prior art keywords
exhaust gas
gas
absorbing liquid
bent portion
gas treatment
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 - Fee Related
Application number
JP536292U
Other languages
Japanese (ja)
Other versions
JPH0560523U (en
Inventor
哲雄 河村
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP536292U priority Critical patent/JP2549604Y2/en
Publication of JPH0560523U publication Critical patent/JPH0560523U/en
Application granted granted Critical
Publication of JP2549604Y2 publication Critical patent/JP2549604Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separating Particles In Gases By Inertia (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案はボイラからの排ガス中の
SOx含有ガスを大気へ放出するまでに除去処理するた
めの排ガス処理装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment apparatus for removing an SOx-containing gas in an exhaust gas from a boiler before releasing the gas to the atmosphere.

【0002】[0002]

【従来の技術】ボイラから排出される排ガス中のSOx
含有ガスを除去処理する従来の排ガス処理装置として
は、図5に示す如きものがある。すなわち、下部位置の
一側に排ガス入口2を設けた所要高さの処理塔1内の上
部位置に、スプレー装置3を多段に配設し、該各段のス
プレー装置3と処理塔1の下端部とを循環ポンプ4、循
環ライン5にて接続し、処理塔1内の吸収液6が循環ポ
ンプ4により循環ライン5より各段のスプレー装置3へ
導かれた後、該スプレー装置3より下向きに噴出される
ようにし、排ガス入口2から処理塔1内に入って上昇す
る排ガスGと上記スプレー装置3から噴出される吸収液
6とが接触させられて脱硫処理が行われるようにしてあ
り、更に、上記スプレー装置3の上方位置には、ミスト
エリミネータ7を設置して、脱硫処理されたガスのミス
ト除去を行うようにしたものがあり、又、塔頂部のガス
放出口8に接続したガス放出ライン9の途中にもミスト
エリミネータ7を設けた構成のものが採用されている。
2. Description of the Related Art SOx in exhaust gas discharged from a boiler
As a conventional exhaust gas treatment apparatus for removing contained gas, there is one as shown in FIG. That is, spray devices 3 are arranged in multiple stages at an upper position in a processing tower 1 having a required height with an exhaust gas inlet 2 provided on one side of a lower position. Are connected with a circulating pump 4 and a circulating line 5, and after the absorbent 6 in the treatment tower 1 is guided from the circulating line 5 to the spray devices 3 in each stage by the circulating pump 4, the liquid flows downward from the spray devices 3 And the exhaust gas G rising from the exhaust gas inlet 2 into the processing tower 1 is brought into contact with the absorbent 6 ejected from the spray device 3 to perform desulfurization treatment. Further, a mist eliminator 7 is provided above the spraying device 3 to remove mist of the desulfurized gas, and a gas mist eliminator 7 is connected to a gas discharge port 8 at the top of the tower. In the middle of release line 9 Those bets eliminator 7 configuration provided is employed.

【0003】[0003]

【考案が解決しようとする課題】ところが、上記従来の
排ガス処理塔の場合は、ガス流れの曲り、急拡大、急縮
小により圧力損失が大きいと共に、ミストエリミネータ
7として高性能のものが1つ又は2つ必要であり、装置
が大きくなり、又、吸収液6のスプレー装置3が多段に
あってヘッドの高さも充分にとってあるため、処理塔1
は背の高い大型のものとなり、設備費が高く、世界的普
及が難しい、等の問題がある。
However, in the case of the above-mentioned conventional exhaust gas treatment tower, the pressure loss is large due to the gas flow bending, rapid expansion, and rapid contraction, and one or more high-performance mist eliminators 7 are used. Since two units are required, the size of the apparatus is large, and the number of spraying apparatuses 3 for the absorbing liquid 6 is multi-stage and the height of the head is sufficiently large.
Are large, tall, expensive, and difficult to spread worldwide.

【0004】そこで、本考案は、上記従来の如き処理塔
に代えて簡単な構成で脱硫とミスト除去ができるような
排ガス処理装置を提供しようとするものである。
Accordingly, the present invention is to provide an exhaust gas treatment apparatus capable of desulfurization and mist removal with a simple configuration instead of the above-mentioned conventional treatment tower.

【0005】[0005]

【課題を解決するための手段】本考案は、上記課題を解
決するために、排ガスダクトを水平状態に配置してガス
流れが横流れとなるようにすると共に、上記排ガスダク
トを水平面内でU字状に折り曲げ、該折曲部の上流側位
置のガス流路に、吸収液噴出用のスプレー装置を、ガス
流れ方向に複数個設置した構成とし、更に、上記折曲部
の底面にホッパーを設け、該ホッパーと上記各スプレー
装置とを循環ポンプ、循環ラインを介し接続した構成と
する。
According to the present invention, in order to solve the above-mentioned problems, the exhaust gas duct is arranged in a horizontal state so that the gas flow becomes a horizontal flow, and the exhaust gas duct is U-shaped in a horizontal plane. In the gas flow path at the upstream side of the bent portion, a plurality of spray devices for ejecting the absorbing liquid are provided in the gas flow direction, and a hopper is provided on the bottom surface of the bent portion. The hopper and each of the spray devices are connected via a circulation pump and a circulation line.

【0006】[0006]

【作用】未処理の排ガスを排ガスダクト内に上流側から
下流側に高速で流すと同時に、各スプレー装置のノズル
からガス流路へ向け吸収液を噴出させると、排ガスはU
字状の折曲部に達する手前で吸収液と接触して脱硫反応
が行われ脱硫処理される。折曲部では遠心力効果により
ミストは外側へ飛ばされて除去される。脱硫され、ミス
トが処理されたガスが下流側から取り出される。
When the untreated exhaust gas flows into the exhaust gas duct at a high speed from the upstream side to the downstream side, and at the same time the absorbing liquid is ejected from the nozzle of each spray device toward the gas flow path, the exhaust gas becomes U
The desulfurization reaction is performed by contact with the absorbing liquid just before reaching the bent portion in the shape of a letter, thereby performing desulfurization treatment. In the bent portion, the mist is blown outward and removed by the centrifugal effect. The gas desulfurized and treated with mist is taken out from the downstream side.

【0007】[0007]

【実施例】以下、図面に基づき本考案の実施例を説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.

【0008】図1乃至図3は本考案の一実施例を示すも
ので、排ガスダクト10を横置きにして水平面内でU字
状に折り曲げ、該折曲部11より一端側を上流側イ、他
端側を下流側ロとして、上流側イから下流側ロへ排ガス
Gを高速で流すようにする。上記折曲部11の上流側位
置の側壁部及び天井部には、ガスの流れ方向に多列とな
るように複数のスプレー装置12を配置して、各列のス
プレー装置12のノズル13をガス流路内に臨ませて脱
硫反応部Aとし、又、折曲部11の底部にはホッパー1
4を設けて吸収液15を貯留できるようにし、該ホッパ
ー14と上記各スプレー装置12とを循環ポンプ16と
循環ライン17により接続して、吸収液15を循環して
使用できるようにすると共に、少なくとも上記折曲部1
1及び脱硫反応部Aを除いて排ガスダクト10の上流側
イ及び下流側ロを斜め上方へ傾斜させて、折曲部11及
び脱硫反応部Aが吸収液15の液溜め部となるようにす
る。
FIGS. 1 to 3 show an embodiment of the present invention, in which an exhaust gas duct 10 is placed horizontally and bent in a U-shape in a horizontal plane, and one end of the bent portion 11 is located on the upstream side. The exhaust gas G is caused to flow at a high speed from the upstream side a to the downstream side b with the other end side as the downstream side b. A plurality of spray devices 12 are arranged on the side wall portion and the ceiling portion on the upstream side of the bent portion 11 so as to be arranged in multiple rows in the gas flow direction. A desulfurization reaction section A is set in the flow path, and a hopper 1 is provided at the bottom of the bent section 11.
4 is provided so that the absorbing liquid 15 can be stored, and the hopper 14 and each of the spray devices 12 are connected by a circulating pump 16 and a circulating line 17 so that the absorbing liquid 15 can be circulated and used. At least the bent part 1
Except for 1 and the desulfurization reaction section A, the upstream side A and the downstream side B of the exhaust gas duct 10 are inclined obliquely upward so that the bent portion 11 and the desulfurization reaction section A become a reservoir for the absorbent 15. .

【0009】なお、上記ノズル13の向きは、ガスの流
れ方向の上流側に向けてガス流と対向流で吸収液15を
噴出できるようにしてもよく、又、ガスの流れ方向と平
行にしてガス流と平行流となるようにしてもよい。又、
流路内に配管を配置し、吸収液をスプレーしてもよい。
The direction of the nozzle 13 may be such that the absorbing liquid 15 can be ejected in a direction opposite to the gas flow toward the upstream side in the gas flow direction. The flow may be parallel to the gas flow. or,
You may arrange | position a piping in a flow path, and may spray an absorption liquid.

【0010】未処理の排ガスGを上流側イから排ガスダ
クト10内に導入して流すと同時に、各スプレー装置1
2に導いた吸収液15をノズル13からガス流路内へ液
滴状又は液膜状に噴出させると、高速で流れる排ガスG
が脱硫反応部Aで吸収液15と接触すると共にガスの流
速によって吸収液15が折曲部11の方へ飛ばされる。
このとき排ガス中の硫黄分は除去されて脱硫処理が行わ
れる。
At the same time as the untreated exhaust gas G is introduced into the exhaust gas duct 10 from the upstream side A and flows therethrough, each spray device 1
2 is ejected from the nozzle 13 into the gas flow path in the form of droplets or liquid film, the exhaust gas G flowing at high speed
Is brought into contact with the absorbing liquid 15 in the desulfurization reaction section A, and the absorbing liquid 15 is blown toward the bent portion 11 by the flow velocity of the gas.
At this time, the sulfur content in the exhaust gas is removed and desulfurization treatment is performed.

【0011】脱硫反応部Aを通過したガス及び該ガスで
運ばれた吸収液15は、U字状に折り曲げてある折曲部
11に達するが、高速のためガスは折曲部11の外側と
なる側壁内面に打ち当てられながら曲げられて下流側ロ
へと流れるので、この折曲部11を通過するときに機械
的、流体力学的にミストの除去が行われる。ガスの流速
を速くすればするほど、ミストの遠心力効果により、ミ
スト除去が効果的に行われる。
The gas passing through the desulfurization reaction section A and the absorbing liquid 15 carried by the gas reach the bent portion 11 bent in a U-shape. Since it is bent while being hit against the inner surface of the side wall and flows downstream, the mist is mechanically and hydrodynamically removed when passing through the bent portion 11. The higher the gas flow rate, the more effectively the mist is removed due to the centrifugal effect of the mist.

【0012】次に、図4は本考案の他の実施例を示すも
ので、折曲部11の前半位置にスプレー装置12を配置
して、この部分を脱硫反応部Aとしたものである。
Next, FIG. 4 shows another embodiment of the present invention, in which a spray device 12 is arranged at a first half position of a bent portion 11, and this portion is used as a desulfurization reaction section A.

【0013】この実施例では、スプレー装置12からガ
ス流路内へ噴出される吸収液の噴出方向を、ガス流れの
上流側の方向へ向けることにより、図示の如く、ガス流
によって吸収液15が折曲部11で押し流され、ガス処
理負荷の大きくなる折曲部11内の外側ゾーンに吸収液
が持ち込まれてガスと吸収液が激しく接触し合うので、
脱硫反応が活発に行われることになる。
In this embodiment, the direction of ejection of the absorbing liquid ejected from the spray device 12 into the gas flow path is directed toward the upstream side of the gas flow, so that the absorbing liquid 15 is formed by the gas flow as shown in the figure. Since the absorbing liquid is brought into the outer zone in the bending part 11 where the gas is loaded by the bending part 11 and the gas processing load becomes large, the gas and the absorbing liquid come into intense contact with each other.
The desulfurization reaction will be actively performed.

【0014】なお、本考案は上記した実施例のみに限定
されるものではなく、たとえば、スプレー装置12の数
は図示以外の数でもよく、又、スプレー装置12の設置
個所は、排ガスダクト10内を流れるガスに吸収液を確
実に接触させることが必要であることから、排ガスダク
ト10の大きさによって決めればよいこと、排ガスダク
ト10の下流側には従来のガス放出ライン上のミストエ
リミネータ7に相当するミストエリミネータは不要にで
きるが、若し設置しても簡易なものでよいこと、等は勿
論である。
The present invention is not limited to the embodiment described above. For example, the number of the spray devices 12 may be other than that shown in the drawing. It is necessary to reliably contact the absorbing liquid with the gas flowing through the exhaust gas duct 10. Therefore, it is necessary to determine the size according to the size of the exhaust gas duct 10. A corresponding mist eliminator can be unnecessary, but it goes without saying that a simple mist eliminator may be used if installed.

【0015】[0015]

【考案の効果】以上述べた如く、本考案の排ガス処理装
置によれば、排ガスダクトを横置きにしてU字状に折り
曲げ、且つ該U字状の折曲部の上流側位置に、ガス流路
と吸収液を噴出させるスプレー装置を設置して、脱硫反
応部とした構成を有するので、次の如き優れた効果を奏
し得る。 (i) 排ガスダクト内を高い流速で流されるガスに対して
スプレー装置から噴出させた吸収液を接触させることに
より、ガスが吸収液を飛散させながら流れる間に脱硫処
理され、反応ゾーンが大きくとれる。 (ii)ガスは排ガスダクト内を流れるだけであるから従来
例に比して圧力損失が小さい。 (iii) 排ガスダクトを横置きする簡単な構成であること
から、既設煙道に設置し易いと共に、設置のための基礎
を小さくできる。 (iv)水平式であるため、循環ポンプヘッドが小さくな
り、運転費を大幅に削減することができる。 (v) 折曲部ではガスの急速旋回運動による遠心力効果に
より、ミスト分離が効果的にでき、下流側へのミストエ
リミネータは不要若しくは簡易なものでよい。 (vi)コンパクトで設備費も小さい。
As described above, according to the exhaust gas treatment apparatus of the present invention, the exhaust gas duct is placed horizontally and bent in a U-shape, and the gas flow is located upstream of the U-shaped bent portion. Since a desulfurization reaction section is provided by installing a channel and a spray device for ejecting the absorbing liquid, the following excellent effects can be obtained. (i) By contacting the gas flowing at a high flow rate in the exhaust gas duct with the absorbing liquid ejected from the spray device, the gas is desulfurized while flowing while scattering the absorbing liquid, so that a large reaction zone can be obtained. . (ii) Since the gas only flows through the exhaust gas duct, the pressure loss is smaller than in the conventional example. (iii) Since the exhaust gas duct has a simple structure in which the exhaust gas duct is placed horizontally, it can be easily installed in the existing flue, and the foundation for installation can be made small. (iv) Since it is a horizontal type, the circulating pump head is small, and the operating cost can be greatly reduced. (v) In the bent portion, mist separation can be effectively performed by the centrifugal force effect of the rapid swirling motion of the gas, and the mist eliminator on the downstream side is unnecessary or simple. (vi) Compact and low equipment cost.

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

【図1】本考案の一実施例を示す平面図である。FIG. 1 is a plan view showing an embodiment of the present invention.

【図2】図1のII−II矢視図である。FIG. 2 is a view taken in the direction of arrows II-II in FIG.

【図3】図2のIII −III 矢視拡大図である。FIG. 3 is an enlarged view taken along a line III-III in FIG. 2;

【図4】本考案の他の実施例を示す部分図である。FIG. 4 is a partial view showing another embodiment of the present invention.

【図5】従来の排ガス処理装置の概略側面図である。FIG. 5 is a schematic side view of a conventional exhaust gas treatment device.

【符号の説明】[Explanation of symbols]

10 排ガスダクト 11 折曲部 12 スプレー装置 14 ホッパー 15 吸収液 16 循環ポンプ 17 循環ライン A 脱硫反応部 イ 上流側 ロ 下流側 G 排ガス DESCRIPTION OF SYMBOLS 10 Exhaust gas duct 11 Bent part 12 Spray device 14 Hopper 15 Absorbent liquid 16 Circulation pump 17 Circulation line A Desulfurization reaction part A Upstream side B Downstream side G Exhaust gas

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 排ガスダクトを横置きにして水平面内で
U字状に折り曲げ、該U字状の折曲部の上流側位置に、
ガス流路へ吸収液を噴出させるスプレー装置を設置して
脱硫反応部とし、且つ上記折曲部の底部に吸収液を溜め
るホッパーを設け、該ホッパーと上記スプレー装置とを
循環ポンプ、循環ラインを介し接続したことを特徴とす
る排ガス処理装置。
An exhaust gas duct is placed horizontally and bent in a U-shape in a horizontal plane, and at an upstream position of the U-shaped bent portion,
A desulfurization reaction section is provided by installing a spray device for ejecting the absorbing liquid into the gas flow path, and a hopper for storing the absorbing liquid is provided at the bottom of the bent portion. An exhaust gas treatment device, wherein the exhaust gas treatment device is connected via a connection.
JP536292U 1992-01-17 1992-01-17 Exhaust gas treatment equipment Expired - Fee Related JP2549604Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP536292U JP2549604Y2 (en) 1992-01-17 1992-01-17 Exhaust gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP536292U JP2549604Y2 (en) 1992-01-17 1992-01-17 Exhaust gas treatment equipment

Publications (2)

Publication Number Publication Date
JPH0560523U JPH0560523U (en) 1993-08-10
JP2549604Y2 true JP2549604Y2 (en) 1997-09-30

Family

ID=11609064

Family Applications (1)

Application Number Title Priority Date Filing Date
JP536292U Expired - Fee Related JP2549604Y2 (en) 1992-01-17 1992-01-17 Exhaust gas treatment equipment

Country Status (1)

Country Link
JP (1) JP2549604Y2 (en)

Also Published As

Publication number Publication date
JPH0560523U (en) 1993-08-10

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