JPH08252426A - Absorption tower - Google Patents

Absorption tower

Info

Publication number
JPH08252426A
JPH08252426A JP7057454A JP5745495A JPH08252426A JP H08252426 A JPH08252426 A JP H08252426A JP 7057454 A JP7057454 A JP 7057454A JP 5745495 A JP5745495 A JP 5745495A JP H08252426 A JPH08252426 A JP H08252426A
Authority
JP
Japan
Prior art keywords
liquid
gas
absorption
storage tank
absorption tower
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
JP7057454A
Other languages
Japanese (ja)
Inventor
Hiroaki Shimazaki
博明 島▲崎▼
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP7057454A priority Critical patent/JPH08252426A/en
Publication of JPH08252426A publication Critical patent/JPH08252426A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE: To prevent a solid from accumulating in a liquid storage tank. CONSTITUTION: This absorption tower sucks a part of an absorption liquid in a lower part liquid storage tank 5 through plural suction apertures 10 while stirring the absorption liquid using a stirrer 6 provided on a wall surface, then drops the atomized absorption liquid from top, and causes the liquid to come into contact with a gas to be treated while, circulating the liquid to absorb and remove sulfur oxides contained in the gas. In this absorption tower, at least one of the plural suction apertures 10 is arranged so that the absorption liquid in the center of the liquid storage tank 5 is sucked.

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、燃焼機器からの排ガス
等の被処理ガスを脱硫処理する吸収塔に係り、特に液溜
タンク内の固形物の堆積を防止する吸収塔に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an absorption tower for desulfurizing a gas to be processed such as exhaust gas from a combustion device, and more particularly to an absorption tower for preventing solids from being accumulated in a liquid tank.

【0002】[0002]

【従来の技術】燃焼機器からの排ガス等の被処理ガス中
に含まれる硫黄酸化物を除去する装置として湿式の排煙
脱硫装置がある。
2. Description of the Related Art There is a wet flue gas desulfurization device as a device for removing sulfur oxides contained in a gas to be treated such as exhaust gas from a combustion device.

【0003】この排煙脱硫装置は、図3及び図4に示す
ように、吸収塔1内で被処理ガスと炭酸カルシウム等の
カルシウム系の吸収剤を含むスラリ状の吸収液とを接触
させて、被処理ガスの脱硫処理を行うものである。吸収
液は、吸収塔1内下部の液溜タンク5に貯留され、この
一部が複数の吸引口11から吸引されて塔1内の上方に
設けられたスプレーノズル8から塔1内に噴霧されて循
環しつつ、塔1内を上昇する被処理ガスと気液接触し
て、ガス中の硫黄酸化物が吸収液に吸収除去される。硫
黄酸化物を吸収した吸収液は液溜タンク5に落下し、こ
の液が側面式の撹拌翼6により撹拌される。循環する吸
収液の一部は抜き出されて酸化処理された後、石こうと
して回収される。
In this flue gas desulfurization apparatus, as shown in FIGS. 3 and 4, the gas to be treated is brought into contact with a slurry-like absorbent containing a calcium-based absorbent such as calcium carbonate in the absorption tower 1. The gas to be treated is desulfurized. The absorption liquid is stored in the liquid storage tank 5 in the lower part of the absorption tower 1, and a part of the absorption liquid is sucked from a plurality of suction ports 11 and sprayed into the tower 1 from a spray nozzle 8 provided above the inside of the tower 1. While being circulated, the sulfur oxide in the gas is absorbed and removed by the absorption liquid by making a gas-liquid contact with the gas to be processed rising in the tower 1. The absorbing liquid that has absorbed the sulfur oxides falls into the liquid storage tank 5, and this liquid is stirred by the side stirring blades 6. A part of the circulating absorption liquid is extracted and oxidized, and then recovered as gypsum.

【0004】[0004]

【発明が解決しようとする課題】ところで、前述の吸収
塔では、図3及び図4に示すように、液溜タンク5(吸
収塔)の周壁に側面式の撹拌機6を配設してタンク内を
撹拌して固形物の堆積を防止するが、タンク5(塔)の
径は15〜20m程であり、タンク5の中央部は撹拌機6に
よる撹拌効果が弱く、すなわち側面式の撹拌機6のみで
はタンクの中央部が淀む。その結果、タンク5の中央部
に固形物が堆積主に石こうが生成されて溜って固まり堆
積し、例えば径3〜4m,高さ2m程の堆積物12とな
る。この堆積物12はメンテナンス時に除去するが、非
常に硬く除去するのに打ち砕くなどかなりの労力が必要
となる。
By the way, in the above-mentioned absorption tower, as shown in FIGS. 3 and 4, a side stirrer 6 is arranged on the peripheral wall of the liquid storage tank 5 (absorption tower) to provide a tank. The inside of the tank 5 (tower) has a diameter of about 15 to 20 m, and the stirring effect by the stirrer 6 is weak in the central portion of the tank 5, that is, a side stirrer. With 6 alone, the center of the tank stagnates. As a result, solid matter is mainly deposited in the central portion of the tank 5, and gypsum is mainly accumulated and accumulated to form a solid matter 12 having a diameter of 3 to 4 m and a height of 2 m, for example. The deposit 12 is removed at the time of maintenance, but it is very hard and requires considerable labor such as crushing to remove it.

【0005】そこで、本発明は、このような実情に鑑み
なされたもので、その目的は、固形物の堆積を防止でき
る吸収塔を提供することにある。
Therefore, the present invention has been made in view of such circumstances, and an object thereof is to provide an absorption tower capable of preventing the accumulation of solid matter.

【0006】[0006]

【課題を解決するための手段】本発明の吸収塔は、下部
の液溜タンク内の吸収液を壁面の撹拌機により撹拌しな
がらその一部を複数の吸引口から吸引して上部から噴霧
落下させて循環させつつ被処理ガスと接触させガス中の
硫黄酸化物を吸収除去する吸収塔において、前記吸引口
の少なくとも1つを、液溜タンク内の中央部の吸収液が
吸引されるように配置したものである。
In the absorption tower of the present invention, while agitating the absorbing liquid in the lower liquid storage tank with a stirrer on the wall surface, a part of it is sucked from a plurality of suction ports and sprayed from the upper part. In an absorption tower that absorbs and removes sulfur oxides in the gas by bringing it into contact with the gas to be treated while circulating it, at least one of the suction ports is adapted to suck the absorption liquid in the central portion of the liquid storage tank. It is arranged.

【0007】[0007]

【作用】液溜タンク内の吸収液は壁面の撹拌機による水
流によって撹拌されるが、撹拌効果はタンクの中央部で
は弱い。このため、吸引口の少なくとも1つを、液溜タ
ンク内の中央部の吸収液が吸引されるように配置するこ
とで、中央部から吸収液が吸引されるため、中央部では
淀みが起こらない。従って、液溜タンク内の固形物の堆
積を防止することが可能となる。
The absorbing liquid in the liquid storage tank is agitated by the water flow by the agitator on the wall surface, but the agitating effect is weak in the central portion of the tank. Therefore, by arranging at least one of the suction ports so that the absorption liquid in the central portion in the liquid storage tank is sucked, the absorption liquid is sucked from the central portion, so that stagnation does not occur in the central portion. . Therefore, it becomes possible to prevent the accumulation of solid matter in the liquid storage tank.

【0008】[0008]

【実施例】以下、本発明の一実施例を添付図面に基づい
て詳述する。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.

【0009】図1及び図2において、1は燃焼機器例え
ばボイラからの排ガス(被処理ガス)を脱硫処理する排
煙脱硫装置の吸収塔を示し、この吸収塔1は例えば竪型
の円筒状に形成され、その側部下方に被処理ガスの導入
口2が設けられていると共に、上部に脱硫処理後のガス
の排出口3が設けられている。
1 and 2, reference numeral 1 denotes an absorption tower of a flue gas desulfurization apparatus for desulfurizing exhaust gas (gas to be treated) from a combustion device such as a boiler. The absorption tower 1 is, for example, a vertical cylindrical shape. An inlet 2 for the gas to be treated is provided below the side portion of the formed gas, and an outlet 3 for the gas after the desulfurization treatment is provided at the top.

【0010】吸収塔1には、被処理ガス中の硫黄酸化物
などの硫黄分を吸収するための炭酸カルシウム等のカル
シウム系の吸収剤が溶解されたスラリ状の吸収液を供給
する吸収液供給管4が接続されていると共に、その内部
下方には吸収液を溜める液溜タンク5が設けられてい
る。液溜タンク5(塔1)の周壁には複数図示例では4
つの撹拌機6が配設され、これら撹拌機6により円周方
向に水流が生じてタンク5内の吸収液が撹拌されるよう
になっている。
The absorption tower 1 is supplied with a slurry-like absorption liquid in which a calcium-based absorbent such as calcium carbonate for absorbing sulfur components such as sulfur oxides in the gas to be treated is dissolved. The pipe 4 is connected, and a liquid storage tank 5 for storing the absorbing liquid is provided below the inside thereof. The peripheral wall of the liquid storage tank 5 (tower 1) has a plurality of 4 in the illustrated example.
One stirrer 6 is provided, and the stirrer 6 causes a water flow in the circumferential direction to stir the absorbing liquid in the tank 5.

【0011】また、液溜タンク5には、タンク5内の吸
収液の一部を循環ポンプ7により塔1内上方に設けられ
たスプレーノズル8に移送する循環管9が接続されてお
り、スプレーノズル8から噴霧された吸収液と塔1内を
上昇する排ガスとが向流気液接触してガス中の硫黄分が
吸収液に吸収除去され、被処理ガスが脱硫処理されるよ
うになっている。スプレーノズル8に吸収液を移送する
循環管9(循環ポンプ7も含む)は、複数(例えば8〜
18)設置され、負荷(被処理ガスの性状等)に応じて
運転台数が任意に決められるようになっている。循環管
9は液溜タンク5の周壁に接続され、それら吸引口10
のうち少なくとも1つ(1又は複数)がタンク5内底部
近傍の中央部又は中央部付近(図1に示す例では中央
部)に配置され、タンク5内底部の中央の吸収液が吸引
されるようになっている。すなわち、任意(1又は複
数)の循環管9をタンク5内底部近傍の中央部又は中央
部付近まで延出する。このように、延出する循環管9に
は常時運転(吸引)される管が含まれるようにする。
尚、図1は分かりやすいように4つの循環管9を液溜タ
ンク5(吸収塔1)に接続した状態を示す図である。
A circulation pipe 9 is connected to the liquid storage tank 5 to transfer a part of the absorption liquid in the tank 5 to a spray nozzle 8 provided in the upper part of the tower 1 by a circulation pump 7. The absorbing liquid sprayed from the nozzle 8 and the exhaust gas rising in the tower 1 come into countercurrent gas-liquid contact, the sulfur content in the gas is absorbed and removed by the absorbing liquid, and the gas to be treated is desulfurized. There is. A plurality of circulation pipes 9 (including the circulation pump 7) for transferring the absorbing liquid to the spray nozzles 8 (for example, 8 to
18) Installed, and the number of operating machines can be arbitrarily determined according to the load (property of the gas to be treated, etc.). The circulation pipe 9 is connected to the peripheral wall of the liquid storage tank 5, and the suction port 10
At least one (one or more) of them is arranged in the central portion near the inner bottom portion of the tank 5 or in the vicinity of the central portion (central portion in the example shown in FIG. 1), and the absorption liquid in the central portion of the inner bottom portion of the tank 5 is sucked. It is like this. That is, an arbitrary (one or more) circulation pipe 9 is extended to the central part in the vicinity of the bottom of the tank 5 or to the vicinity of the central part. Thus, the extending circulation pipe 9 includes a pipe that is constantly operated (sucked).
Note that FIG. 1 is a diagram showing a state in which four circulation pipes 9 are connected to a liquid storage tank 5 (absorption tower 1) for easy understanding.

【0012】次に本実施例の作用を述べる。Next, the operation of this embodiment will be described.

【0013】排ガス(被処理ガス)は、導入口2から吸
収塔1内に導入され、塔1内を上昇する。この吸収塔1
には、例えば炭酸カルシウムの吸収剤が溶解されたスラ
リ状の吸収液が吸収液供給管4から導入され、液溜タン
ク5内に溜まる。その一部が循環ポンプ7により循環管
9を介してスプレーノズル8に移送され、そのノズル8
から塔1内に噴霧落下する。この吸収液とガスとが向流
接触してガス中の硫黄酸化物などの硫黄分が吸収液に吸
収され、被処理ガスが脱硫処理される。脱硫処理された
ガスは、排出口3から排出されて他の系に導かれる。
Exhaust gas (gas to be treated) is introduced into the absorption tower 1 through the inlet 2 and rises in the tower 1. This absorption tower 1
For example, a slurry-like absorption liquid in which an absorption agent of calcium carbonate is dissolved is introduced from the absorption liquid supply pipe 4 and accumulated in the liquid storage tank 5. A part thereof is transferred to the spray nozzle 8 via the circulation pipe 9 by the circulation pump 7, and the nozzle 8
Spray down into the tower 1. The absorbing liquid and the gas are countercurrently contacted with each other so that the sulfur content such as sulfur oxides in the gas is absorbed by the absorbing liquid, and the gas to be treated is desulfurized. The desulfurized gas is discharged from the discharge port 3 and guided to another system.

【0014】脱硫処理後の吸収液は、塔1内を落下して
液溜タンク5に溜まり、一部は適宜抜き出されて酸化処
理された後石こうとして回収される。このタンク5内の
吸収液が撹拌機6による円周方向の水流により撹拌さ
れ、この水流が強いところでは問題ないが、水流が弱い
と固形分が堆積する。この水流が弱いところすなわち撹
拌効果が弱いところとはタンク5中央部であり、この中
央部の底部近傍には循環管9の吸引口10が配置されて
いる。これにより、中央部の液が吸引口10から吸引さ
れるため、撹拌効果が弱くても中央部では淀みが起こら
ない。従って、液溜タンク5内の固形物の堆積を防止す
ることができる。これによって堆積物がなくなるので、
定検時等のメンテナンスが容易となる。
After the desulfurization treatment, the absorbing liquid falls in the tower 1 and collects in the liquid storage tank 5. A part of the absorbing liquid is appropriately extracted and oxidized, and then recovered as gypsum. The absorbing liquid in the tank 5 is agitated by the water flow in the circumferential direction by the agitator 6, and there is no problem in a place where the water flow is strong, but when the water flow is weak, solid content is accumulated. The place where the water flow is weak, that is, the place where the stirring effect is weak is the center of the tank 5, and the suction port 10 of the circulation pipe 9 is arranged near the bottom of the center. As a result, the liquid in the central portion is sucked from the suction port 10, so that stagnation does not occur in the central portion even if the stirring effect is weak. Therefore, it is possible to prevent the accumulation of solid matter in the liquid storage tank 5. This will remove the deposits,
Maintenance such as regular inspections becomes easy.

【0015】[0015]

【発明の効果】以上要するに本発明によれば、液溜タン
ク内の固形物の堆積を防止できるという優れた効果を奏
する。
In summary, according to the present invention, the excellent effect of preventing the accumulation of solid matter in the liquid storage tank can be obtained.

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

【図1】本発明の一実施例を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of the present invention.

【図2】吸収塔の一例を示す構成図である。FIG. 2 is a configuration diagram showing an example of an absorption tower.

【図3】吸収塔内の底部中央部に固形物が堆積した状態
を例を図である。
FIG. 3 is a diagram showing an example of a state in which solid matter is accumulated in the center of the bottom of the absorption tower.

【図4】図3のA−A線矢視図である。FIG. 4 is a view taken along the line AA of FIG.

【符号の説明】[Explanation of symbols]

1 吸収塔 5 液溜タンク 6 撹拌機 10 吸引口 1 Absorption tower 5 Liquid storage tank 6 Stirrer 10 Suction port

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 下部の液溜タンク内の吸収液を壁面の撹
拌機により撹拌しながらその一部を複数の吸引口から吸
引して上部から噴霧落下させて循環させつつ被処理ガス
と接触させガス中の硫黄酸化物を吸収除去する吸収塔に
おいて、前記吸引口の少なくとも1つを、液溜タンク内
の中央部の吸収液が吸引されるように配置したことを特
徴とする吸収塔。
1. While stirring the absorbing liquid in the lower liquid storage tank by means of a stirrer on the wall surface, a part of the liquid is sucked from a plurality of suction ports, sprayed and dropped from the upper part, and circulated so as to come into contact with the gas to be treated. In an absorption tower that absorbs and removes sulfur oxides in gas, at least one of the suction ports is arranged so that the absorption liquid in the central portion of the liquid storage tank is sucked.
JP7057454A 1995-03-16 1995-03-16 Absorption tower Pending JPH08252426A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7057454A JPH08252426A (en) 1995-03-16 1995-03-16 Absorption tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7057454A JPH08252426A (en) 1995-03-16 1995-03-16 Absorption tower

Publications (1)

Publication Number Publication Date
JPH08252426A true JPH08252426A (en) 1996-10-01

Family

ID=13056123

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7057454A Pending JPH08252426A (en) 1995-03-16 1995-03-16 Absorption tower

Country Status (1)

Country Link
JP (1) JPH08252426A (en)

Similar Documents

Publication Publication Date Title
US5665317A (en) Flue gas scrubbing apparatus
RU96102565A (en) INSTALLATION OF A WET TYPE FOR SULFURING FUEL GASES AND A METHOD FOR USING A SOLID SULFURIZING SUBSTANCE
WO2007080676A1 (en) Wet flue gas desulfurization apparatus
JPH08108035A (en) Wet fuel gas desulfurizer
JPH0938456A (en) Wet flue gas desulfurizer
JP3735977B2 (en) Flue gas desulfurization equipment
JP3621159B2 (en) Exhaust gas treatment method and apparatus
TW201132404A (en) Exhaust gas treatment device
JPH08252426A (en) Absorption tower
CN215388639U (en) Integrated dust removal desulfurization tower
JPS6134026Y2 (en)
JP2003103139A (en) Wet process flue gas desulfurizer
JPH0866613A (en) Absorption tower
JPH09141050A (en) Method for washing inside of gas absorber of smoke desulfirization plant and device therefor
JPH0533828U (en) Absorption tower of flue gas desulfurization equipment
JPS6246424Y2 (en)
JP3942778B2 (en) Wet flue gas desulfurization equipment
JP4349511B2 (en) Exhaust gas treatment device and operation method thereof
JP2002153727A (en) Double chamber type wet flue gas desulfurization device
JPH11207145A (en) Air blowing device for flue gas desulfurization equipment
CN217247957U (en) Desulfurization, denitration, dedusting and dehydration integrated equipment
JP3590856B2 (en) Exhaust gas desulfurization method
JP3388984B2 (en) Flue gas treatment equipment
JPS6134027Y2 (en)
JP3842706B2 (en) Wet flue gas desulfurization apparatus and method

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040226

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040309

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20040706