JPS6325810B2 - - Google Patents
Info
- Publication number
- JPS6325810B2 JPS6325810B2 JP54019405A JP1940579A JPS6325810B2 JP S6325810 B2 JPS6325810 B2 JP S6325810B2 JP 54019405 A JP54019405 A JP 54019405A JP 1940579 A JP1940579 A JP 1940579A JP S6325810 B2 JPS6325810 B2 JP S6325810B2
- Authority
- JP
- Japan
- Prior art keywords
- tower
- side wall
- duct
- absorption tower
- absorption
- 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
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
【発明の詳細な説明】
本発明は、吸収塔に関し、特に石灰等のスラリ
を吸収液として用いる湿式排煙脱硫装置に用いる
のに好適な吸収塔に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an absorption tower, and more particularly to an absorption tower suitable for use in a wet flue gas desulfurization device that uses slurry such as lime as an absorption liquid.
湿式脱硫装置に用いられる吸収塔は、従来第1
図のように塔内にスプレ手段2を有し、このスプ
レ手段2の設置個所より下方に位置する塔側壁に
ガス導入用ダクト3を設けられている。このよう
な吸収塔において、石灰石および石灰を吸収剤と
するスラリは、スプレ手段2から噴霧され、ダク
ト3から導入された排ガス中に含されるSO2ガス
と接触する。この際問題となることは、吸収塔の
ガス入口部付近において、吸収剤スラリが導入さ
れたガスによつてドライアツプされるとともにガ
ス中のSO2ガスにより吸収剤スラリのPHが低下す
るためスケールが発生することである。このスケ
ールは、特に塔内を流下してダクト3と吸収塔と
の連結部付近に付着しやすくなる。このためにダ
クト内の通風損失が大きくなり、安定したガス吸
収操作が困難となる。 The absorption tower used in wet desulfurization equipment has traditionally been
As shown in the figure, a spray means 2 is provided in the tower, and a gas introduction duct 3 is provided on the side wall of the tower located below the location where the spray means 2 is installed. In such an absorption tower, limestone and a slurry containing lime as an absorbent are sprayed from the spray means 2 and come into contact with SO 2 gas contained in the exhaust gas introduced from the duct 3. The problem in this case is that near the gas inlet of the absorption tower, the absorbent slurry is dried up by the introduced gas, and the pH of the absorbent slurry decreases due to the SO 2 gas in the gas, causing scale. It is something that happens. This scale particularly tends to flow down inside the tower and adhere to the vicinity of the connection between the duct 3 and the absorption tower. This increases ventilation loss within the duct, making stable gas absorption operations difficult.
本発明は、上記した従来技術の欠点を除去し、
吸収塔にガスを導入するダクトと吸収塔側壁部と
の連結部付近におけるスケーリングを防止して、
安定したガス吸収操作を行うことができる吸収塔
を提供することにある。 The present invention eliminates the drawbacks of the prior art described above,
By preventing scaling near the connection between the duct that introduces gas into the absorption tower and the side wall of the absorption tower,
An object of the present invention is to provide an absorption tower capable of performing stable gas absorption operations.
要するに、ダクトの底面部と吸収塔側壁との連
結部を、塔内を流下するスラリの落下地点より離
すようにダクトと塔側壁の連結部付近の形状を改
良せしめたものである。 In short, the shape of the vicinity of the connection between the duct and the tower side wall has been improved so that the connection between the bottom of the duct and the absorption tower side wall is separated from the drop point of the slurry flowing down inside the tower.
以下、本発明を添付図面に示す実施例によりさ
らに詳しく説明する。 Hereinafter, the present invention will be explained in more detail with reference to embodiments shown in the accompanying drawings.
第2図に示す吸収塔は、吸収塔本体1内にスプ
レ手段2が設けられ、このスプレ手段の設置個所
より下方に位置する塔側壁にガス導入用ダクト3
が設けられている。このダクトの上面部と塔側壁
との連結部aと、ダクトの底面部と塔側壁との連
結部bとは、連結部bが連結部aよりも吸収塔本
体1の中心軸から遠方に位置するような関係にな
つている。連結部bより下方に延びる塔側壁部4
は、ダクトを設けていない他方の塔側壁部5とほ
ぼ対称の形状を有し、排出管6に接続している。 The absorption tower shown in FIG. 2 includes a spraying means 2 in the absorption tower main body 1, and a gas introduction duct 3 on the side wall of the tower located below the installation point of the spraying means.
is provided. The connection part a between the top surface of the duct and the tower side wall and the connection part b between the bottom surface of the duct and the tower side wall are such that the connection part b is located further from the central axis of the absorption tower main body 1 than the connection part a. We have a relationship where we do things like that. Tower side wall portion 4 extending downward from the connecting portion b
has a shape that is almost symmetrical to the other tower side wall 5 which is not provided with a duct, and is connected to the discharge pipe 6.
第3図に示す吸収塔は、連結部aと連結部bと
は第2図に示す吸収塔と同様の位置関係にあり、
連結部bより下方に延びる塔側壁部7の形状が第
2図に示す吸収塔の場合と異なつている。塔側壁
部7は連結部bから吸収塔本体1の中心軸側に下
方に傾斜し、この塔側壁部7に続く塔側壁部8は
傾斜度を減じて下方に延び排出部6と接続してい
る。 In the absorption tower shown in FIG. 3, the connection part a and the connection part b are in the same positional relationship as in the absorption tower shown in FIG.
The shape of the tower side wall portion 7 extending downward from the connecting portion b is different from that of the absorption tower shown in FIG. The column side wall section 7 is inclined downward from the connecting section b toward the central axis of the absorption column main body 1, and the column side wall section 8 following this column side wall section 7 reduces the degree of inclination and extends downward to connect with the discharge section 6. There is.
上記スプレ手段としては、一般にスプレノズル
を多数設けたパイプが用いられる。スプレノズル
の向きは上方でも下方でもよい。また前記した連
結部aと連結部bの位置関係は相対的なものであ
つて、厳密に一定の数値で関係づけられる必要は
なく、吸収塔本体1の内径、スプレ手段2の設置
個所、ダクト3の径、などによる構造上の条件ま
たはガス吸収操作上の条件に適宜選定できる。さ
らに連結部bから下方に延びる塔側壁部の形状
は、塔内を流入するスラリがスムーズに排出管6
まで到達しやすいように設計されたものであれば
よく特に制約されない。したがつて連結部bから
下方に延びる塔側壁部の断面形状を彎曲状として
も差支えない。 As the above-mentioned spray means, generally a pipe provided with a large number of spray nozzles is used. The spray nozzle may be oriented upward or downward. Furthermore, the positional relationship between the connecting portion a and the connecting portion b described above is relative, and does not need to be strictly related by a fixed value. It can be selected as appropriate depending on the structural conditions or the gas absorption operation conditions, such as the diameter of No. 3. Furthermore, the shape of the tower side wall extending downward from the connecting part b allows the slurry flowing into the tower to flow smoothly into the discharge pipe 6.
There are no particular restrictions as long as it is designed so that it can be easily reached. Therefore, the cross-sectional shape of the tower side wall portion extending downward from the connecting portion b may be curved.
以上のような構成からなる吸収塔において、
SO2を含む排ガスは、ダクト3から吸収塔本体1
内に導入されて塔内を上昇し、スプレ手段2から
供給された吸収剤スラリと接触反応する。この接
触反応によつて吸収剤スラリは、亜硫酸カルシウ
ムまたは二水石膏を反応生成物として含有し、塔
内を流下する。しかしダクト3の底面部と塔側壁
との連結部bが流下するスラリの落下地点よりダ
クト側に位置しているから、流下するスラリはダ
クト3の底面部に付着することなく、吸収塔1の
下部を形成する塔側壁部に落下する。 In the absorption tower having the above configuration,
The exhaust gas containing SO 2 is transferred from the duct 3 to the absorption tower main body 1.
The absorbent slurry is introduced into the column, rises inside the column, and reacts in contact with the absorbent slurry supplied from the spray means 2. As a result of this contact reaction, the absorbent slurry contains calcium sulfite or gypsum dihydrate as a reaction product and flows down the column. However, since the connecting part b between the bottom of the duct 3 and the tower side wall is located closer to the duct than the falling point of the slurry flowing down, the slurry flowing down does not adhere to the bottom of the duct 3 and can be removed from the absorption tower 1. It falls onto the side wall of the tower forming the lower part.
以上、本発明を湿式排煙脱硫装置に用いた吸収
塔について説明したが、本発明は、同様なスケー
ルが問題となる他の吸収塔にも同様に適用するこ
とができる。 Although the present invention has been described above regarding an absorption tower used in a wet flue gas desulfurization apparatus, the present invention can be similarly applied to other absorption towers in which similar scale is a problem.
本発明によれば、吸収塔へのガス導入口付近、
特に塔側壁に連接するダクト底面部のスケーリン
グが防止できるため、ガス導入用ダクトの通風損
失を低下させることなく、安定したガス吸収操作
を行うことができる。 According to the present invention, near the gas inlet to the absorption tower,
In particular, since scaling of the bottom portion of the duct connected to the tower side wall can be prevented, stable gas absorption operation can be performed without reducing the ventilation loss of the gas introduction duct.
第1図は従来の吸収塔の構造を示す概略的構造
図、第2図は本発明の一実施例を示す概略的構造
図、第3図は本発明の他の実施例を示す概略的構
造図である。
1……吸収塔本体、2……スプレ手段、3……
ダクト、a……連結部(ダクト上面部と塔側壁
部)、b……連結部(ダクト底面部と塔側壁部)。
Fig. 1 is a schematic structural diagram showing the structure of a conventional absorption tower, Fig. 2 is a schematic structural diagram showing one embodiment of the present invention, and Fig. 3 is a schematic structural diagram showing another embodiment of the present invention. It is a diagram. 1... Absorption tower main body, 2... Spray means, 3...
Duct, a... Connecting part (duct top part and tower side wall part), b... Connecting part (duct bottom part and tower side wall part).
Claims (1)
2の設置個所より下方に位置する塔側壁にガス導
入用ダクト3を設けた吸収塔において、前記ダク
ト3の底面部と塔側壁との連結部bを、前記ダク
ト3の上面部と塔側壁との連結部aよりも吸収塔
本体1の中心軸から遠方にあるように吸収塔側壁
4にダクト3を設けたことを特徴とする吸収塔。1. In an absorption tower having a spray means 2 in the tower and a gas introduction duct 3 provided on the tower side wall located below the installation location of the spray means 2, the connection between the bottom part of the duct 3 and the tower side wall An absorption tower characterized in that the duct 3 is provided on the absorption tower side wall 4 such that the part b is located further from the central axis of the absorption tower main body 1 than the connecting part a between the upper surface part of the duct 3 and the tower side wall. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1940579A JPS55111823A (en) | 1979-02-21 | 1979-02-21 | Absorbing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1940579A JPS55111823A (en) | 1979-02-21 | 1979-02-21 | Absorbing tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55111823A JPS55111823A (en) | 1980-08-28 |
| JPS6325810B2 true JPS6325810B2 (en) | 1988-05-26 |
Family
ID=11998342
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1940579A Granted JPS55111823A (en) | 1979-02-21 | 1979-02-21 | Absorbing tower |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS55111823A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3989465A (en) * | 1973-03-07 | 1976-11-02 | American Air Filter Company, Inc. | Apparatus for controlling reaction conditions in a sulfur dioxide scrubber |
| JPS5523656B2 (en) * | 1973-11-30 | 1980-06-24 |
-
1979
- 1979-02-21 JP JP1940579A patent/JPS55111823A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55111823A (en) | 1980-08-28 |
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