JPH11319480A - Stack-integrated flue gas desulfurizer - Google Patents
Stack-integrated flue gas desulfurizerInfo
- Publication number
- JPH11319480A JPH11319480A JP10156689A JP15668998A JPH11319480A JP H11319480 A JPH11319480 A JP H11319480A JP 10156689 A JP10156689 A JP 10156689A JP 15668998 A JP15668998 A JP 15668998A JP H11319480 A JPH11319480 A JP H11319480A
- Authority
- JP
- Japan
- Prior art keywords
- mist
- flange
- stack
- absorption tower
- exhaust gas
- 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
【0001】[0001]
【発明の属する技術分野】本発明は排ガス中に含まれる
硫黄酸化物を除去する排煙脱硫装置、特に煙突一体型排
煙脱硫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 a flue gas desulfurization apparatus for removing sulfur oxides contained in exhaust gas, and more particularly to a stack-integrated flue gas desulfurization apparatus.
【0002】[0002]
【従来の技術】ボイラ等の排ガスには硫黄酸化物が含ま
れており、硫黄酸化物は酸性雨の原因となる等、大気汚
染の要因であるので、排ガスの排出にあたって排煙脱硫
装置により硫黄酸化物が除去されている。産業用の排煙
脱硫装置としては煙突一体型排煙脱硫装置が有り、煙突
を流通する排ガスにアルカリ性の中和剤を投入して脱硫
を行っている。この脱硫過程で発生した同伴ミストを除
去する為、煙突一体型排煙脱硫装置内部にはミストエリ
ミネータが設けられている。2. Description of the Related Art Exhaust gas from boilers and the like contains sulfur oxides, which cause air pollution such as acid rain. The oxide has been removed. As an industrial flue gas desulfurization device, there is a stack exhaust gas desulfurization device, in which an alkaline neutralizing agent is added to exhaust gas flowing through the chimney to perform desulfurization. A mist eliminator is provided inside the stack-integrated flue gas desulfurization device to remove the entrained mist generated in this desulfurization process.
【0003】図3により従来の煙突一体型排煙脱硫装置
について説明する。Referring to FIG. 3, a conventional flue gas desulfurization apparatus integrated with a chimney will be described.
【0004】煙突一体型排煙脱硫装置は吸収塔1の上端
に煙突2が連設された構成となっている。[0004] The stack-integrated flue gas desulfurization apparatus has a structure in which a stack 2 is connected to the upper end of an absorption tower 1.
【0005】前記吸収塔1の下部には吸収液の貯留部3
が形成され、該貯留部3の上方には多数のスプレーノズ
ル4が配設され、該スプレーノズル4は吸収液供給管5
により前記貯留部3に連通し、又吸収液供給管5には循
環ポンプ6が設けられている。前記スプレーノズル4の
上方、貯留部3の出口近傍には排ガス中のミストを捕集
するミストエリミネータ7が設けられている。In the lower part of the absorption tower 1, a storage part 3 for absorbing liquid is provided.
Is formed, and a large number of spray nozzles 4 are disposed above the storage section 3.
Thus, a circulation pump 6 is provided in the absorption liquid supply pipe 5. A mist eliminator 7 for collecting mist in the exhaust gas is provided above the spray nozzle 4 and near the outlet of the storage unit 3.
【0006】該ミストエリミネータ7は、ジクザク状に
屈曲成形した薄板を所要の間隙を設けて多数重合させた
ものであり、排ガスが屈曲した狭隘な間隙を通過するこ
とで排ガス中の同伴ミストを捕集している。The mist eliminator 7 is formed by laminating a large number of thin plates bent in a zigzag shape with a predetermined gap provided therebetween, and traps entrained mist in the exhaust gas by passing through the narrow gap where the exhaust gas is bent. Gathering.
【0007】石炭焚ボイラ等から煙道(図示せず)を通
過し、排ガス入口8から吸収塔1に送出された排ガス
は、前記スプレーノズル4より噴霧される吸収液と接触
することで硫黄酸化物(S02 )が吸収除去される。更
に、前記ミストエリミネータ7を通過する過程で排ガス
中に含まれる同伴ミストが除去され、前記煙突2を上昇
して大気へ放出される。[0007] Exhaust gas that has passed through a flue (not shown) from a coal-fired boiler or the like and that has been sent from the exhaust gas inlet 8 to the absorption tower 1 comes into contact with the absorbing liquid sprayed from the spray nozzle 4 to thereby oxidize sulfur. object (S0 2) is absorbed and removed. Further, entrained mist contained in the exhaust gas is removed in the process of passing through the mist eliminator 7, and rises up the chimney 2 and is discharged to the atmosphere.
【0008】又、前記吸収塔1を出た排ガス中にはある
程度の水分が含まれており、その水分は前記煙突2内壁
面に付着し、凝縮水9として流下し、排ガスの流速が速
くなる前記吸収塔1と前記煙突2との接続部に於いて、
上昇する前記排ガスにより前記凝縮水9が吹上げられて
再飛散し、煙突の上端からミストとして周囲へ飛散する
ことがあった。この為、煙突2の上端部には有底リング
状の受部材10を取付け、該受部材10によってミスト
を捕集すると共に該受部材10の底部に捕集したミスト
をドレイン管11により貯留部3に戻している。Further, the exhaust gas that has exited the absorption tower 1 contains a certain amount of moisture, and the moisture adheres to the inner wall surface of the chimney 2 and flows down as condensed water 9 to increase the flow rate of the exhaust gas. At the connection between the absorption tower 1 and the chimney 2,
In some cases, the condensed water 9 was blown up by the rising exhaust gas and scattered again, and scattered as mist from the upper end of the chimney to the surroundings. For this reason, a bottomed ring-shaped receiving member 10 is attached to the upper end of the chimney 2, and the mist collected by the receiving member 10 is collected by the drain tube 11 into a storage part. Returned to 3.
【0009】[0009]
【発明が解決しようとする課題】然し乍ら上記受部材1
0は煙突2の内壁面を流下する凝縮水9が吹上げられて
再飛散するという根本的な解決策ではなく、更に受部材
10は煙突2の上端から飛沫する比較的粒子の大きなミ
ストは捕捉できるが、粒子の小さなミスト或は排ガスと
共に流出するミストの捕捉はできない。However, the receiving member 1 described above.
0 is not a fundamental solution that the condensed water 9 flowing down the inner wall surface of the chimney 2 is blown up and re-scattered, and the receiving member 10 captures a relatively large mist of particles that are sprayed from the upper end of the chimney 2. It can, but cannot capture small mist of particles or mist flowing out with exhaust gas.
【0010】更に又、排ガス中のミストを完全に除去す
る為には前記ミストエリミネータ7のミスト捕集率を高
める必要があるが、捕集率を高めた場合ミストエリミネ
ータ7での圧力損失が大きくなり、排ガスの所定の流速
が得られないと言う問題があり、煙突2より排出される
排ガスからミストを充分に除去することが困難であっ
た。更に、この種の煙突一体型排煙脱硫装置から排出さ
れる排ガスの温度は略50℃であり排ガス中の硫化物、
水蒸気は凝縮してミスト化するが、煙突中で凝縮した硫
化物、水蒸気の除去は更に困難であった。Furthermore, in order to completely remove the mist in the exhaust gas, it is necessary to increase the mist collection rate of the mist eliminator 7. However, when the collection rate is increased, the pressure loss in the mist eliminator 7 becomes large. Therefore, there is a problem that a predetermined flow rate of the exhaust gas cannot be obtained, and it has been difficult to sufficiently remove the mist from the exhaust gas discharged from the chimney 2. Further, the temperature of the exhaust gas discharged from this type of stack-integrated flue gas desulfurization device is approximately 50 ° C.
Water vapor condenses and forms a mist, but it is more difficult to remove sulfide and water vapor condensed in the chimney.
【0011】本発明は斯かる実情に鑑み、煙突の内壁面
を流下する凝縮水が吹上げられて再飛散するのを防止す
ると共に排ガス中のミストを積極的に捕集し、排出され
る排ガスに含まれるミストを大幅に低減しようとするも
のである。In view of such circumstances, the present invention prevents condensed water flowing down the inner wall surface of a chimney from being blown up and re-scattered, and also actively collects mist in the exhaust gas and discharges the exhaust gas. It is intended to significantly reduce the mist contained in the mist.
【0012】[0012]
【課題を解決するための手段】本発明は、内部にスプレ
ーノズル、ミストエリミネータが設けられた吸収塔の上
端に煙突が連設される煙突一体型排煙脱硫装置に於い
て、吸収塔の前記ミストエリミネータの上側の位置に押
込フランジを設けると共に該押込フランジに対向して吸
引フランジを設け、該吸引フランジより吸引した排ガス
を前記押込フランジより噴出し、吸収塔を上昇する排ガ
スに旋回流を発生させ、前記煙突内壁面の所要位置にミ
スト捕集樋を設けた煙突一体型排煙脱硫装置に係り、又
前記吸引フランジからの吸引方向、前記押込フランジか
らの噴出方向が前記吸収塔壁面の接線方向である煙突一
体型排煙脱硫装置に係り、更に又前記押込フランジに対
して前記吸引フランジが下側に位置する煙突一体型排煙
脱硫装置に係るものであり、排ガスに旋回流を与えるこ
とで前記煙突を上昇する過程で排ガス中のミストが煙突
内壁面に衝突して液滴化し、煙突内壁面を流下して前記
ミスト捕集樋に捕集される。SUMMARY OF THE INVENTION The present invention relates to a stack-integrated flue gas desulfurization apparatus in which a chimney is connected to the upper end of an absorption tower provided with a spray nozzle and a mist eliminator therein. A pushing flange is provided at a position above the mist eliminator, and a suction flange is provided opposite to the pushing flange. Exhaust gas sucked from the suction flange is ejected from the pushing flange to generate a swirl flow in the exhaust gas rising in the absorption tower. The present invention relates to a stack-integrated flue gas desulfurization device provided with a mist collecting gutter at a required position on the inner wall surface of the chimney, and the direction of suction from the suction flange and the direction of ejection from the pushing flange are tangent to the wall surface of the absorption tower. The invention relates to a stack-integrated flue gas desulfurization device, wherein the suction flange is located below the pushing flange. In the process of raising the chimney by giving a swirl flow to the exhaust gas, mist in the exhaust gas collides with the inner wall surface of the chimney to form droplets, flows down the inner wall surface of the chimney and is collected by the mist collecting gutter. .
【0013】[0013]
【発明の実施の形態】以下、図面を参照しつつ本発明の
実施の形態を説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0014】図1は本実施の形態の要部の概略を示すも
のであり、図1に於いて図3中で示したものと同様のも
のには同符号を付し、説明を省略する。FIG. 1 schematically shows a main part of the present embodiment. In FIG. 1, the same components as those shown in FIG. 3 are denoted by the same reference numerals, and description thereof will be omitted.
【0015】前記吸収塔1の上端には煙突2が連設さ
れ、該煙突2は下半部に対して上半部が細径となってい
る。又、吸収塔1と煙突2との接合部1a、及び前記煙
突2の下半部と上半部との接合部2aはテーパ状となっ
ている。A chimney 2 is connected to the upper end of the absorption tower 1, and the diameter of the chimney 2 in the upper half is smaller than that in the lower half. Further, a junction 1a between the absorption tower 1 and the chimney 2 and a junction 2a between the lower half and the upper half of the chimney 2 are tapered.
【0016】前記吸収塔1の前記ミストエリミネータ7
より上側、前記接合部1aより下側に旋回流発生装置1
5が設けられる。The mist eliminator 7 of the absorption tower 1
Above the swirl flow generator 1 below the joint 1a.
5 are provided.
【0017】図2により該旋回流発生装置15を説明す
る。The swirling flow generator 15 will be described with reference to FIG.
【0018】吸収塔1の外周接線方向に押込フランジ1
6、吸引フランジ17を相対向させ設け、該吸引フラン
ジ17は前記押込フランジ16に対して上下方向の位置
が下側となっている。該押込フランジ16、吸引フラン
ジ17と吸収塔1の中心に関して反対勝手にもう1組の
押込フランジ18、吸引フランジ19を設ける。In the tangential direction of the outer circumference of the absorption tower 1
6. The suction flanges 17 are provided so as to face each other, and the position of the suction flange 17 in the vertical direction with respect to the pushing flange 16 is on the lower side. Another pair of the pushing flange 18 and the suction flange 19 are provided opposite to each other with respect to the pushing flange 16, the suction flange 17 and the center of the absorption tower 1.
【0019】一方の組の押込フランジ16と他方の組の
吸引フランジ19とを旋回流発生ブロア21を介して連
通し、一方の組の吸引フランジ17と他方の組の押込フ
ランジ18とをもう1つの旋回流発生ブロア22を介し
て連通する。而して、前記旋回流発生ブロア21、旋回
流発生ブロア22はそれぞれ吸引フランジ17、吸引フ
ランジ19より吸収塔1内の排ガスを吸引し、前記押込
フランジ16、押込フランジ18より吸収塔1内に噴出
する。One set of pushing flanges 16 and the other set of suction flanges 19 communicate with each other via a swirling flow generating blower 21, and one set of suction flanges 17 and the other set of pushing flanges 18 are connected to one another. The two swirling flow generating blowers 22 communicate with each other. Thus, the swirling flow generating blower 21 and the swirling flow generating blower 22 suck the exhaust gas in the absorption tower 1 from the suction flange 17 and the suction flange 19, respectively, and enter the absorption tower 1 from the pushing flange 16 and the pushing flange 18. Gushing.
【0020】前記煙突2の下半部の下部内壁面で、前記
接合部1aの上側に全周に亘り、第1ミスト捕集樋23
を設け、又前記煙突2の上半部の下部内壁面で前記接合
部2aの上側に全周に亘り、第2ミスト捕集樋24を設
ける。該第2ミスト捕集樋24及び前記第1ミスト捕集
樋23にミストドレイン管25を連通させ、該ミストド
レイン管25の下端は貯留部3に連通する。On the lower inner wall surface of the lower half of the chimney 2 and over the joint 1a, the first mist collecting gutter 23 extends all around.
In addition, a second mist collecting gutter 24 is provided on the lower inner wall surface of the upper half portion of the chimney 2 and above the joint portion 2a over the entire circumference. A mist drain pipe 25 communicates with the second mist collection gutter 24 and the first mist collection gutter 23, and a lower end of the mist drain pipe 25 communicates with the storage unit 3.
【0021】以下、作動について説明する。Hereinafter, the operation will be described.
【0022】石炭焚ボイラ等から煙道(図示せず)を通
過し、排ガス入口8から吸収塔1に送出された排ガス
は、前記スプレーノズル4より噴霧される吸収液と接触
することで硫黄酸化物(S02 )が吸収除去され、ミス
トエリミネータ7を通過する。該ミストエリミネータ7
を通過する過程で排ガス中に含まれるミストの大部分が
が除去される。Exhaust gas that has passed through a flue (not shown) from a coal-fired boiler or the like and has been sent to the absorption tower 1 from an exhaust gas inlet 8 comes into contact with the absorbing liquid sprayed from the spray nozzle 4 to thereby oxidize sulfur. object (S0 2) are absorbed and removed, it passes through the mist eliminator 7. The mist eliminator 7
Most of the mist contained in the exhaust gas is removed in the process of passing through.
【0023】前記した様に、前記旋回流発生ブロア21
により吸引フランジ19より排ガスが吸引され、吸引さ
れた排ガスは前記押込フランジ16より噴出され、同様
に前記旋回流発生ブロア22により吸引フランジ17よ
り排ガスが吸引され、吸引された排ガスは前記押込フラ
ンジ18より噴出され、前記吸収塔1内部の内壁面に沿
った反対勝手の2つの接線流が形成され、該接線流によ
り吸収塔1内部に図2中反時計方向の旋回流27が惹起
される。As described above, the swirl flow generating blower 21
The exhaust gas is sucked from the suction flange 19, and the sucked exhaust gas is ejected from the pushing flange 16. Similarly, the exhaust gas is sucked from the suction flange 17 by the swirling flow generating blower 22, and the sucked exhaust gas is sucked into the pushing flange 18. The two tangential flows are formed to blow out along the inner wall surface inside the absorption tower 1, and the tangential flows generate a swirling flow 27 counterclockwise in FIG. 2 inside the absorption tower 1.
【0024】尚、上記した様に押込フランジ16,18
に対して吸引フランジ17,19の位置を下側にずら
せ、更に吸収塔1内の排ガスは上昇しているので、前記
吸引フランジ17,19から吸引されるガスは前記押込
フランジ16,18から噴出したガスとは異なる。従っ
て、ガスの噴出と吸引により、上昇する排ガスに対して
有効に旋回流を発生させることができる。又、同様な理
由で前記押込フランジ16と前記押込フランジ18、前
記吸引フランジ17と前記吸引フランジ19についても
上下位置をずらせてもよい。As described above, the pushing flanges 16, 18
The positions of the suction flanges 17 and 19 are shifted to the lower side, and the exhaust gas in the absorption tower 1 further rises, so that the gas sucked from the suction flanges 17 and 19 is ejected from the pushing flanges 16 and 18. Is different from the gas used. Therefore, the swirling flow can be effectively generated for the rising exhaust gas by ejecting and sucking the gas. For the same reason, the pushing flange 16 and the pushing flange 18 and the suction flange 17 and the suction flange 19 may be shifted vertically.
【0025】該旋回流27は前記接合部1aにより排ガ
ス流が絞られることで速度を増し高速の旋回流となり、
前記接合部2aにより更に絞られることで更に高速の旋
回流となる。この旋回流27により脱硫過程で発生した
同伴ミスト、煙突内で凝縮したミストを煙突2の内壁面
に衝突させる。ミストは衝突により液滴化し、凝縮水9
となって煙突2の内壁面を流下し、前記第1ミスト捕集
樋23、第2ミスト捕集樋24に捕集され、更に前記ミ
ストドレイン管25より前記貯留部3に戻される。而し
て、煙突2からはミストが充分に除去された排ガスが排
出される。The swirling flow 27 is increased in speed by the exhaust gas flow being throttled by the joint 1a, and becomes a high-speed swirling flow.
A further high-speed swirling flow is obtained by further narrowing down by the joint 2a. The entrained mist generated in the desulfurization process and the mist condensed in the chimney by the swirling flow 27 collide with the inner wall surface of the chimney 2. The mist is turned into droplets by collision and condensed water 9
As a result, the gas flows down the inner wall surface of the chimney 2, is collected by the first mist collection gutter 23 and the second mist collection gutter 24, and is further returned to the storage unit 3 from the mist drain pipe 25. Thus, exhaust gas from which mist has been sufficiently removed is discharged from the chimney 2.
【0026】又、凝縮水9は前記第2ミスト捕集樋2
4、第1ミスト捕集樋23に捕集されるので、従来の様
に、前記吸収塔1と前記煙突2との接続部に於いて、前
記凝縮水9が上昇する排ガスにより吹上げられて再飛散
することがない。The condensed water 9 is supplied to the second mist collecting gutter 2
4. Since the water is collected by the first mist collecting gutter 23, the condensed water 9 is blown up by the rising exhaust gas at the connection between the absorption tower 1 and the chimney 2 as in the related art. No re-scattering.
【0027】尚、上記実施の形態では吸引フランジ、押
込フランジを2組設けたが、1組であっても、或は3組
以上であってもよい。又、煙突2の径を2段とし途中に
接合部2aを設けたが、径を1段とし接合部2aは必ず
しも設ける必要はない。更に、ミスト捕集樋は1つであ
っても、3つ以上であってもよい。In the above embodiment, two sets of suction flanges and push-in flanges are provided, but one set or three or more sets may be provided. Further, although the diameter of the chimney 2 is set to two steps and the joint 2a is provided in the middle, the diameter of the chimney 2 is set to one step and the joint 2a is not necessarily provided. Furthermore, the number of mist collecting gutters may be one, or three or more.
【0028】又、上記した旋回流発生装置15は煙突2
の外部から取付けるので現存の煙突一体型排煙脱硫装置
に追加設備が可能であると共に装置運転中でも改造、追
加設備が可能である。The above-mentioned swirling flow generator 15 is provided with the chimney 2
Since it is installed from outside, the existing stack-integrated flue gas desulfurization unit can be equipped with additional equipment, and can be modified or added even during operation of the equipment.
【0029】[0029]
【発明の効果】以上述べた如く本発明によれば、煙突を
上昇する排ガスに圧損を与えることなく旋回流を付与で
きるので、効果的に排ガス中のミストの捕集ができ、排
出される排ガスに含まれるミストを大幅に低減すること
ができると共に旋回流を付与する装置は現存の煙突一体
型排煙脱硫装置に追加設備可能であると共に運転中にも
追加工事が可能であるという優れた効果を発揮する。As described above, according to the present invention, a swirl flow can be imparted to the exhaust gas rising in the chimney without causing a pressure loss, so that mist in the exhaust gas can be effectively collected and the exhaust gas discharged The device that can significantly reduce the mist contained in the gas and add the swirl flow can be added to the existing stack-integrated flue gas desulfurization device, and it is possible to perform additional work during operation. Demonstrate.
【図1】本発明の実施の形態の要部を示す概略図であ
る。FIG. 1 is a schematic diagram showing a main part of an embodiment of the present invention.
【図2】該実施の形態に設けられる旋回流発生装置の概
略図である。FIG. 2 is a schematic diagram of a swirling flow generator provided in the embodiment.
【図3】従来例を示す概略図である。FIG. 3 is a schematic view showing a conventional example.
1 吸収塔 2 煙突 4 スプレーノズル 7 ミストエリミネータ 15 旋回流発生装置 16 押込フランジ 17 吸引フランジ 18 押込フランジ 19 吸引フランジ 23 第1ミスト捕集樋 24 第2ミスト捕集樋 25 ミストドレイン管 27 旋回流 DESCRIPTION OF SYMBOLS 1 Absorption tower 2 Chimney 4 Spray nozzle 7 Mist eliminator 15 Swirling flow generator 16 Pushing flange 17 Suction flange 18 Pushing flange 19 Suction flange 23 1st mist collection gutter 24 2nd mist collection gutter 25 Mist drain pipe 27 Swirl flow
Claims (3)
ータが設けられた吸収塔の上端に煙突が連設される煙突
一体型排煙脱硫装置に於いて、吸収塔の前記ミストエリ
ミネータの上側の位置に押込フランジを設けると共に該
押込フランジに対向して吸引フランジを設け、該吸引フ
ランジより吸引した排ガスを前記押込フランジより噴出
し、吸収塔を上昇する排ガスに旋回流を発生させ、前記
煙突内壁面の所要位置にミスト捕集樋を設けたことを特
徴とする煙突一体型排煙脱硫装置。1. A stack-integrated flue gas desulfurization system in which a chimney is connected to an upper end of an absorption tower provided with a spray nozzle and a mist eliminator therein, and is pushed into a position above the mist eliminator in the absorption tower. A flange is provided and a suction flange is provided opposite to the pushing flange. Exhaust gas sucked from the suction flange is blown out from the pushing flange to generate a swirl flow in the exhaust gas rising in the absorption tower, and the required chimney inner wall surface is formed. A stack-integrated flue gas desulfurization device characterized by providing a mist collecting gutter at a position.
押込フランジからの噴出方向が前記吸収塔壁面の接線方
向である請求項1の煙突一体型排煙脱硫装置。2. The stack-integrated flue gas desulfurization apparatus according to claim 1, wherein a suction direction from the suction flange and a jetting direction from the pushing flange are tangential to a wall surface of the absorption tower.
ンジが下側に位置する請求項1の煙突一体型排煙脱硫装
置。3. The flue gas desulfurization apparatus integrated with a chimney according to claim 1, wherein the suction flange is located below the pushing flange.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10156689A JPH11319480A (en) | 1998-05-21 | 1998-05-21 | Stack-integrated flue gas desulfurizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10156689A JPH11319480A (en) | 1998-05-21 | 1998-05-21 | Stack-integrated flue gas desulfurizer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11319480A true JPH11319480A (en) | 1999-11-24 |
Family
ID=15633186
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10156689A Pending JPH11319480A (en) | 1998-05-21 | 1998-05-21 | Stack-integrated flue gas desulfurizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11319480A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100357014C (en) * | 2006-01-06 | 2007-12-26 | 易晓辉 | Chimney desulfurizing tower integrated desulfurizing process and apparatus thereof |
JP2011179767A (en) * | 2010-03-02 | 2011-09-15 | Nippon Electric Glass Co Ltd | Exhaust gas treatment device and exhaust gas treatment method |
CN102641647A (en) * | 2012-04-13 | 2012-08-22 | 金川集团有限公司 | Recovery processing method for low-concentration stray smoke S02 |
CN102994170A (en) * | 2011-09-19 | 2013-03-27 | 于恩常 | Power-superposition swirl-type desulfurizing tower |
JP2013185754A (en) * | 2012-03-08 | 2013-09-19 | Shizuoka Seiki Co Ltd | Exhaust structure of electric dryer |
WO2017159099A1 (en) * | 2016-03-15 | 2017-09-21 | 富士電機株式会社 | Exhaust gas processing device |
WO2022049917A1 (en) * | 2020-09-04 | 2022-03-10 | 富士電機株式会社 | Exhaust gas treatment device |
CN117247795A (en) * | 2023-11-17 | 2023-12-19 | 山西晋南钢铁集团有限公司 | Coke oven gas desulfurizing tower |
-
1998
- 1998-05-21 JP JP10156689A patent/JPH11319480A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100357014C (en) * | 2006-01-06 | 2007-12-26 | 易晓辉 | Chimney desulfurizing tower integrated desulfurizing process and apparatus thereof |
JP2011179767A (en) * | 2010-03-02 | 2011-09-15 | Nippon Electric Glass Co Ltd | Exhaust gas treatment device and exhaust gas treatment method |
CN102994170A (en) * | 2011-09-19 | 2013-03-27 | 于恩常 | Power-superposition swirl-type desulfurizing tower |
JP2013185754A (en) * | 2012-03-08 | 2013-09-19 | Shizuoka Seiki Co Ltd | Exhaust structure of electric dryer |
CN102641647A (en) * | 2012-04-13 | 2012-08-22 | 金川集团有限公司 | Recovery processing method for low-concentration stray smoke S02 |
WO2017159099A1 (en) * | 2016-03-15 | 2017-09-21 | 富士電機株式会社 | Exhaust gas processing device |
JP2019076798A (en) * | 2016-03-15 | 2019-05-23 | 富士電機株式会社 | Exhaust gas treatment equipment |
WO2022049917A1 (en) * | 2020-09-04 | 2022-03-10 | 富士電機株式会社 | Exhaust gas treatment device |
CN117247795A (en) * | 2023-11-17 | 2023-12-19 | 山西晋南钢铁集团有限公司 | Coke oven gas desulfurizing tower |
CN117247795B (en) * | 2023-11-17 | 2024-02-02 | 山西晋南钢铁集团有限公司 | Coke oven gas desulfurizing tower |
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