JPS61178020A - Apparatus for absorbing exhaust gas - Google Patents

Apparatus for absorbing exhaust gas

Info

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
Application number
JP60021354A
Other languages
Japanese (ja)
Inventor
Toshikatsu Suzuki
敏勝 鈴木
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP60021354A priority Critical patent/JPS61178020A/en
Publication of JPS61178020A publication Critical patent/JPS61178020A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

PURPOSE:To increase an absorbing speed by performing the recirculation of an absorbing solution at a sufficiently high speed, in an inverted scrubber, by enclosing a gas-liquid contact part and the absorbing solution reflux pipe from a tower top in an absorbing tower. CONSTITUTION:Exhaust gas is introduced into an absorbing tower 2 from a blower 1 and contacted with the absorbing solution, which is blown up from an absorbing solution storage tank 4 by air blow pressure, in a gas-liquid contact part 3 having a Venturi throat, a perforated plate and a packing material to remove the harmful component in the gas while the treated gas is receives gas-liquid separation treatment in a gas-liquid separation chamber 5 and exhausted from the outlet 8 of the absorbing tower 2 through a demister 7. The absorbing solution is flowed down from the gas-liquid separation chamber 5 by the absorbing solution reflux pipe 6 enclosed in the absorbing tower 2 to be returned to the absorbing solution storage tank 4.

Description

【発明の詳細な説明】[Detailed description of the invention]

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.

【図面の簡単な説明】[Brief explanation of the drawing]

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)

【特許請求の範囲】[Claims] ガス吸収塔側面より排ガスを導入し吸収塔下部より吸収
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.
JP60021354A 1985-02-05 1985-02-05 Apparatus for absorbing exhaust gas Pending JPS61178020A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
US3739551A (en) Method of gas absorption and apparatus therefor
JPH10216476A (en) Waste gas treatment and apparatus therefor
Chung et al. Dehumidification of moist air with simultaneous removal of selected indoor pollutants by triethylene glycol solutions in a packed-bed absorber
JPS6336817A (en) Wet flue gas purifying method and device therefor
US3944402A (en) Air pollution control apparatus and process
JPH0372913A (en) Method and apparatus for treating exhaust gas
JPH02290218A (en) Gas absorption tower
CN102049167B (en) High-SO2 concentration pressure smoke desulfuration method and device
KR100484563B1 (en) A scrubber apparatus for processing noxious gases and fine dusts simultaneously
US4487748A (en) Process for treating exhaust gases
KR0136645B1 (en) Method and apparatus for treating waste gas
JPS61178020A (en) Apparatus for absorbing exhaust gas
CN210740445U (en) Bubble film treatment equipment for waste incineration flue gas purification
CN207856650U (en) A kind of spray scattering tower
CN105999938A (en) Flue gas treatment device capable of recycling heat
KR20100122740A (en) Cyclon scrubber for ship and gas treatment method thereof
CN205965447U (en) Optical excitation electrolysis is device of SOx/NOx control demercuration simultaneously
CN106039913B (en) A kind of flue gas purification system
US3919389A (en) Method of purifying air containing mercury vapor
RU2440839C2 (en) Heat exchanger (desorber-absorber)
WO1992012786A1 (en) Stripping method and apparatus
CN110841444A (en) Integrated device and process for simultaneously desulfurizing and denitrifying flue gas by liquid phase method
CN218485192U (en) Industrial waste gas purification treatment system
JPH0699026A (en) Treatment of waste gas
JPH09262433A (en) Cooling absorber for high temperature harmful gas and method thereof