JPS61178020A - Apparatus for absorbing exhaust gas - Google Patents
Apparatus for absorbing exhaust gasInfo
- Publication number
- JPS61178020A JPS61178020A JP60021354A JP2135485A JPS61178020A JP S61178020 A JPS61178020 A JP S61178020A JP 60021354 A JP60021354 A JP 60021354A JP 2135485 A JP2135485 A JP 2135485A JP S61178020 A JPS61178020 A JP S61178020A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- absorbing
- absorption
- tower
- liquid
- 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.)
- Pending
Links
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
Description
本発明は排ガス吸収装置に関するものである。従来湿式
方法による排ガス吸収装置には、排ガスと吸収液を流す
方向として並流式と向流式とがある。向流式排ガス吸収
装置においては、排ガスの流れる方向とは逆方向に吸収
液を流して、充填物、多孔板、ベンチュリースロート等
の気液接触機構を介して排ガス中の有害成分を吸収除去
する方法である。並流式排ガス吸収装置は、排ガス流と
同一方向に吸収液を流し上述の気液接触機構を介して排
ガス中の有害成分を除去する方法である。並流式吸収装
置は処理ガス量が一般に向流式吸収装置に比して大きく
とれる結果、設備費が向流式吸収装置に比して著しく小
さい。又並流式吸収装置の中には、吸収液を排ガスの送
風圧により塔頂あるいは塔底部に吹き上げ、又は吸引し
て吹ぎ下げる様式の吸収装置もあり、こうした様式の吸
収装置においては、吸収液移送ポンプが無いため装置の
設置面積は著しく小さい。本発明の方法も同じく並流式
吸収装置に属するものであるが、並流式吸収装置の特徴
を更に進めて考案したものである。
本発明の吸収装置においては、吸収液はガスの送入圧力
によって吸収塔内のペンチュリースq −ト、多孔板、
充填物等 ある気液接触部に吹き上げられるが、吸収塔
塔頂の気液分離室内で気液分離された吸収液は、吸収塔
外部に出ることなく、吸収塔内部に設置された吸収液還
流管を通って迅速に吸収液貯留槽内に還流する。吸収液
の還流管が吸収塔外に出ない構造は本発明の特徴とする
ものである。本発明の装置においては、吸収液の循環は
十分迅速に行なわれる結果、有害ガス吸収速度が大きく
、又吸収塔そのものがコンパクトになる。又本発明の吸
収装置においては、従来最も装置占有面積の小さな並流
式吸収装置と同様にポンプが不要であるためのポンプお
よびポンプ配管の占有する空間が不要であるばかりか、
吸収液の還流管が吸収塔外に出ていないので、装置の占
有する空間は、従来のどの吸収装置よりも小さい。これ
は排ガス吸収装置を設置する場合重要なことである。化
学工場はもとより化学実験室のドラフト、団地・商店等
の浄化槽等に設置する場合でも、小さな許容空間しかな
い場合が多い。父上にドラフト等の装置に組み込む場合
に本発明の装置の特徴である吸収培体に吸収液の還流管
が露出していないということは重要なことである。
本発明を図面により説明する。
排ガスは、送風機(1)により吸収塔(2)内部に導入
され、ベンチュリースロート、多孔板、充填物等のある
気液接触部(3)で、吸収液貯留槽(4)から送風圧に
より吹き上がった吸収液と接触し有害成分を除去され、
気液分離室(5)で気液分離され、吸収液還流管(6)
により流下して吸収液貯留槽(4)にもどる。排ガスは
デミスタ−(7)を経て吸収塔出口(8)がら排出され
る。The present invention relates to an exhaust gas absorption device. Conventional wet-type exhaust gas absorption devices include a parallel-flow type and a counter-current type in which the exhaust gas and absorption liquid are allowed to flow. In a counter-current exhaust gas absorption device, the absorption liquid flows in the opposite direction to the flow direction of the exhaust gas, and harmful components in the exhaust gas are absorbed and removed through gas-liquid contact mechanisms such as packing, perforated plates, and venturi throats. It's a method. The parallel flow type exhaust gas absorption device is a method in which an absorption liquid is caused to flow in the same direction as the exhaust gas flow, and harmful components in the exhaust gas are removed through the above-mentioned gas-liquid contact mechanism. As a result of the fact that the amount of gas to be processed in a co-current absorber is generally larger than that in a counter-current absorber, the equipment cost is significantly lower than that in a counter-current absorber. Also, among the co-current absorption devices, there are absorption devices in which the absorption liquid is blown up to the top or bottom of the tower by the blowing pressure of exhaust gas, or is sucked and blown down. Since there is no liquid transfer pump, the footprint of the device is significantly smaller. Although the method of the present invention also belongs to the co-current type absorption apparatus, it has been devised by further advancing the features of the co-current type absorption apparatus. In the absorption apparatus of the present invention, the absorption liquid is transferred to the penturi sq-seat, perforated plate, and
Packing materials, etc.Although the absorption liquid is blown up to a certain gas-liquid contact part, the absorption liquid separated into gas and liquid in the gas-liquid separation chamber at the top of the absorption tower does not flow out of the absorption tower, but instead flows into the absorption liquid reflux system installed inside the absorption tower. It quickly refluxes into the absorbent reservoir through the tube. The structure in which the absorption liquid reflux pipe does not come out of the absorption tower is a feature of the present invention. In the apparatus of the present invention, the absorption liquid is circulated sufficiently quickly, so that the harmful gas absorption rate is high and the absorption tower itself is compact. In addition, in the absorption device of the present invention, as with the conventional parallel flow type absorption device which occupies the smallest device area, there is no need for a pump, so the space occupied by the pump and pump piping is not only unnecessary.
Since the absorption liquid reflux pipe does not exit the absorption tower, the space occupied by the device is smaller than that of any conventional absorption device. This is important when installing an exhaust gas absorption device. In many cases, there is only a small allowable space for installation, not only in chemical factories, but also in chemical laboratory fume hoods, septic tanks in housing complexes, shops, etc. When the device is incorporated into a device such as a fume hood, it is important that the reflux tube for the absorption liquid is not exposed to the absorption medium, which is a feature of the device of the present invention. The present invention will be explained with reference to the drawings. Exhaust gas is introduced into the absorption tower (2) by a blower (1), and is blown from the absorption liquid storage tank (4) by blowing pressure at the gas-liquid contact area (3), which has a venturi throat, perforated plate, packing, etc. Harmful components are removed by contact with the rising absorption liquid,
Gas and liquid are separated in the gas-liquid separation chamber (5), and the absorption liquid is returned to the reflux pipe (6).
The liquid flows down and returns to the absorption liquid storage tank (4). The exhaust gas passes through a demister (7) and is discharged from the absorption tower outlet (8).
【実施例1 】
亜硫酸ガス300岬を含むドラフト排ガスを多孔板3段
を気液接触装置に使用してガス流速10m/secで送
り、吸収液としては炭酸ナトリウム1%を用い、液ガス
比測定の結果、0.51 / mで運転した結果、亜硫
酸ガス除去率は、99.8%であった。[Example 1] Draft exhaust gas containing 300 sulfur dioxide gas was sent at a gas flow rate of 10 m/sec using three stages of perforated plates as a gas-liquid contact device, and 1% sodium carbonate was used as the absorption liquid to measure the liquid-gas ratio. As a result, the sulfur dioxide gas removal rate was 99.8% when operated at 0.51/m.
図は吸収装置の概略図である。 The figure is a schematic diagram of the absorption device.
Claims (1)
塔内部に設置したベンチュリースロート、多孔板および
充填物に吸収液を排ガスの送風圧により吹き上げて気液
接触せしめる通常の倒立スクラバーにおいて、気液接触
部および塔頂よりの吸収液還流管を吸収塔に内包するこ
とを特徴とする排ガス吸収装置In a normal inverted scrubber, exhaust gas is introduced from the side of the gas absorption tower and from the lower part of the absorption tower, the absorption liquid is blown up by the blowing pressure of the exhaust gas to the Venturi throat, perforated plate, and packing installed inside the absorption tower to bring them into gas-liquid contact. An exhaust gas absorption device characterized in that an absorption tower includes a contact portion and an absorption liquid reflux pipe from the top of the tower.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60021354A JPS61178020A (en) | 1985-02-05 | 1985-02-05 | Apparatus for absorbing exhaust gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60021354A JPS61178020A (en) | 1985-02-05 | 1985-02-05 | Apparatus for absorbing exhaust gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61178020A true JPS61178020A (en) | 1986-08-09 |
Family
ID=12052760
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60021354A Pending JPS61178020A (en) | 1985-02-05 | 1985-02-05 | Apparatus for absorbing exhaust gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61178020A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102974193A (en) * | 2012-12-24 | 2013-03-20 | 上海建安化工设计有限公司 | Tail gas absorbing tower |
CN103785116A (en) * | 2013-12-20 | 2014-05-14 | 台州恒之泰医化设备有限公司 | Gas respirator |
-
1985
- 1985-02-05 JP JP60021354A patent/JPS61178020A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102974193A (en) * | 2012-12-24 | 2013-03-20 | 上海建安化工设计有限公司 | Tail gas absorbing tower |
CN103785116A (en) * | 2013-12-20 | 2014-05-14 | 台州恒之泰医化设备有限公司 | Gas respirator |
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