JPH05245327A - Exhaust gas desulfurization dust removing device - Google Patents

Exhaust gas desulfurization dust removing device

Info

Publication number
JPH05245327A
JPH05245327A JP4084931A JP8493192A JPH05245327A JP H05245327 A JPH05245327 A JP H05245327A JP 4084931 A JP4084931 A JP 4084931A JP 8493192 A JP8493192 A JP 8493192A JP H05245327 A JPH05245327 A JP H05245327A
Authority
JP
Japan
Prior art keywords
exhaust gas
unit
outlet
exhaust
tank
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
JP4084931A
Other languages
Japanese (ja)
Inventor
Toshio Yamamoto
利雄 山本
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 JP4084931A priority Critical patent/JPH05245327A/en
Publication of JPH05245327A publication Critical patent/JPH05245327A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To effectively perform exhaust gas treatment with good efficiency and without contaminating environment when gas temp. is high and when harmful gas is simultaneously removed by treating exhaust gas by a desulfurization dust removing device which a dehumidifying unit using waste heat, a washing dust removal unit and a purifying unit are combined to form. CONSTITUTION:In a tank 1 having a suction opening 2 and an exhaust opening 3 of exhaust gas is installed a dehumidifying unit using waste heat A where purified gas flows in and out to perform heat giving and receiving. In the poststage a washing dust removal unit B which communicates with the exhaust opening 3 and where a separation tank 10 equipped with an inlet 11, an outlet 12 and a water tank 18 is provided and where a nozzle 27 turned diagonally backwards and a shielding wall plate 15 are arranged on the inner wall and near the outlet 12 of the separation tank 10, respectively. The outlet 12 communicates with an inflow opening 6 to circulate the exhaust gas through the units A, B. Further, a water tank 8 and the nozzle 27 of the unit B communicate with a purifying unit C having a filter 25 which is attachable and detachable through a pump 32.

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、ガス温度が高い場合や
有害ガスも同時に除去したい場合に適した排気ガス脱硫
除塵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 an exhaust gas desulfurization dust remover suitable for high gas temperatures and for removing harmful gases at the same time.

【0002】[0002]

【従来の技術】産業の発達は工場,鉱山,交通機関等か
らの汚染物質の量を増大させ、一方、都市の発達は、家
庭,事務所等から放散される汚染物質の量を増加させ、
大気汚染は公衆衛生上,また経済上からも重要な問題に
なってきた。
2. Description of the Related Art Industrial development increases the amount of pollutants from factories, mines, transportation facilities, etc., while urban development increases the amount of pollutants emitted from homes, offices, etc.
Air pollution has become an important issue for public health and economic reasons.

【0003】大気の主要な汚染源は燃料の燃焼による排
気ガスにより発生するもので、燃料の燃焼に際して発生
し、大気を汚染する主要な物質は、固体としては、石
炭,コークスの微粒子,炭素またはすすの微粒子,及び
灰分であり、液体または半固体としてはタール状物質の
粒子,無水硫酸のミストであり、ガスとしては炭化水
素,一酸化炭素,窒素酸化物,亜硫酸ガス等である。
The main pollutant of the atmosphere is generated by the exhaust gas generated by the combustion of fuel, and the main substances that are generated during the combustion of fuel and pollute the atmosphere are solids such as coal, fine particles of coke, carbon or soot. Particles and ash, liquid or semi-solid particles of tar-like substances, sulfuric acid mist, and gases such as hydrocarbons, carbon monoxide, nitrogen oxides, and sulfurous acid gas.

【0004】しかして従来は上記のような排気ガスの温
度が高い場合や有害ガスを含む場合に適した排気ガス洗
浄集塵装置としては、普通、洗浄液微粒化部,気体接触
部,気液分離部,固液ため部からなる排気ガス洗浄集塵
装置が多種多様の形式で知られている。
However, conventionally, as an exhaust gas cleaning and dust collecting apparatus suitable for the case where the temperature of the exhaust gas is high and the case where the harmful gas is contained, a cleaning liquid atomizing section, a gas contact section, a gas-liquid separation are usually used. Exhaust gas cleaning dust collectors consisting of a solid part and a solid liquid part are known in various types.

【0005】[0005]

【発明が解決しようとする課題】しかし従来の洗浄集塵
装置ではミスト除去器やあとの排水処理が必要であると
共に排ガス温度が下がるので、煙突からのガス拡散が悪
くなり、環境の汚染濃度が高くなるなどの問題があっ
た。
However, in the conventional cleaning and dust collecting apparatus, a mist remover and subsequent waste water treatment are required, and the exhaust gas temperature is lowered, so that the gas diffusion from the chimney is deteriorated and the pollutant concentration in the environment is reduced. There was a problem such as getting expensive.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
するためになされたものであって、次のように構成して
ある。以下、図1,2に示す各実施例について図面を参
照しながら詳しく説明する。
The present invention has been made to solve the above problems, and is configured as follows. Hereinafter, each embodiment shown in FIGS. 1 and 2 will be described in detail with reference to the drawings.

【0007】[0007]

【実施例】先ずAは、前後に排気ガスの吸込,排気口
2,3を有するタンク1内の排気ガス流路Sを囲繞して
該排気ガスと熱授受を行う浄化ガスの流入,出口6,7
を有する熱交換器構成の排熱利用除湿ユニットである。
なお該排熱利用除湿ユニットAは、タンク1内の排気ガ
ス室である前部室4と後部室5とが複数本の連通管8で
それぞれ連通され、この各連通管8が排気ガス流路Sを
構成している。またタンク1内には、流入口6及び流出
口7を仕切る垂下板9が中央部に垂設され洗浄ガスの迂
回流路を形成している。次にBは、上記の排気口3に連
通する前部入口11と後部出口12を有すると共に出口
12下方に水槽18を備えた分離タンク10内の内壁に
斜後方(下方)向きのノズル27を設けてその後方(下
方)の出口12近傍に先端に複数の寸断切欠堰板16を
有する遮壁板15が設けられた出口12を排熱利用除湿
ユニットAの流入口6に連通させてなる洗浄集塵ユニッ
トである。なお、図1において14は後部室、17は通
孔である。また19は水槽18の排水口で、20はドレ
ン抜きである。さらにCは、通入口22及び通出口23
を有する掩蓋24付きの処理タンク21内に着脱自在の
濾過器25が支板26上に載設されてなる浄化ユニット
である。そして該浄化ユニットCは、その処理タンク2
1の通入口22が排水管30によって洗浄集塵ユニット
Bの排水口19に接続され、また同通出口23がポンプ
32介装の送水管31によって洗浄集塵ユニットBのノ
ズル27に接続されている。なお29は通気管、33は
排気管、34,35はバッフルである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, A is an inlet / outlet 6 of a purified gas which surrounds an exhaust gas flow path S in a tank 1 having front and rear exhaust gas inlets and exhaust ports 2 and 3 for exchanging heat with the exhaust gas. , 7
Is a dehumidification unit utilizing exhaust heat having a heat exchanger configuration.
In the exhaust heat utilizing dehumidification unit A, the front chamber 4 and the rear chamber 5 which are exhaust gas chambers in the tank 1 are respectively communicated by a plurality of communication pipes 8, and each of the communication pipes 8 is connected to the exhaust gas passage S. Is composed of. Further, in the tank 1, a hanging plate 9 for partitioning the inflow port 6 and the outflow port 7 is vertically installed at a central portion to form a bypass passage for the cleaning gas. Next, B has a nozzle 27 facing obliquely backward (downward) on the inner wall of the separation tank 10 having a front inlet 11 and a rear outlet 12 communicating with the exhaust port 3 and having a water tank 18 below the outlet 12. Cleaning in which the outlet 12 provided with a barrier plate 15 having a plurality of cutout weir plates 16 at the tip thereof in the vicinity of the outlet 12 at the rear (lower side) of the outlet 12 is communicated with the inlet 6 of the dehumidification unit A using exhaust heat. It is a dust collection unit. In FIG. 1, 14 is a rear chamber and 17 is a through hole. Further, 19 is a drain port of the water tank 18, and 20 is a drain port. Further, C is the entrance 22 and the exit 23.
It is a purification unit in which a detachable filter 25 is mounted on a support plate 26 in a processing tank 21 with a cover 24 having a. The purification unit C is the processing tank 2
The inlet 22 of No. 1 is connected to the drain 19 of the cleaning and dust collecting unit B by the drain pipe 30, and the outlet 23 is connected to the nozzle 27 of the cleaning and dust collecting unit B by the water pipe 31 of the pump 32. There is. In addition, 29 is a ventilation pipe, 33 is an exhaust pipe, and 34 and 35 are baffles.

【0008】[0008]

【作用】先ずポンプ32を稼働して浄化ユニットCの処
理タンク21内の濾過処理水をノズル27に圧送し、該
ノズル27より洗浄水を洗浄集塵ユニットBの分離タン
ク10内に斜後方(下方)向き矢印方向28に噴射させ
る。そして汚染された高温の排気ガス(例えばジーゼル
自動車の排気ガス)を排熱利用除湿ユニットAのタンク
1の吸込口2から吸込み、排気口3から次の洗浄集塵ユ
ニットBの分離タンク10内へ入口11から送込み、出
口12から排出する。しかしてこの際、分離タンク10
内を前(上)方から後(下)方へ流れる排気ガスにはノ
ズル27から洗浄水が噴射され、水との接触によって排
気ガス混在の粉塵,各種塵埃などは比重を増し、下方の
水槽18内へ沈降する。この場合、排ガス中の大気汚染
の元凶ともいうべき有害排ガスの最たるSOχも水によ
って吸収除去される。そして上記水との接触で洗浄され
た洗浄ガスは遮壁板15の先端部を迂回して出口12か
ら排気管33を経て流入口6から排熱利用除湿ユニット
Aのタンク1内に入り、各連通管8と接触して各連通管
8を流れる高温の排気ガスとの間で熱授受(熱交換)が
行われて洗浄ガスは暖められると共に除湿されて流出口
7から外気中へ排出される。また洗浄集塵ユニットBの
水槽18内に溜った水は排水管30を経て浄化ユニット
Cの処理タンク21内へ移送されて濾過器25によって
自動的に濾過、清浄化される。そしてこの清浄化された
水はポンプ32によって送水管31を経て洗浄集塵ユニ
ットBのノズル27へ圧送され排気ガスの洗浄集塵に繰
返し使用される。また濾過器25は適宜脱外、引上げら
れて粉塵,塵埃,夾雑物などの混在物は廃棄処理され
る。
First, the pump 32 is operated to pump the filtered treated water in the treatment tank 21 of the purification unit C to the nozzle 27, and the washing water is obliquely rearwardly fed into the separation tank 10 of the washing and dust collecting unit B from the nozzle 27 ( The fuel is jetted in the downward direction 28. Then, the polluted high-temperature exhaust gas (for example, exhaust gas of diesel automobile) is sucked from the suction port 2 of the tank 1 of the exhaust heat utilizing dehumidification unit A, and from the exhaust port 3 into the separation tank 10 of the next cleaning and dust collecting unit B. It is fed from the inlet 11 and discharged from the outlet 12. However, at this time, the separation tank 10
Cleaning water is jetted from the nozzle 27 to the exhaust gas flowing from the front (upper) to the rear (lower), and the dust and various dusts mixed with the exhaust gas increase in specific gravity due to contact with the water, and the lower water tank. Settle into 18. In this case, SO χ, which is the most harmful exhaust gas in the exhaust gas, which is considered to be a source of air pollution, is also absorbed and removed by water. Then, the cleaning gas cleaned by contact with the water bypasses the tip portion of the barrier plate 15 and enters the tank 1 of the dehumidifying unit A using exhaust heat from the outlet 12 through the exhaust pipe 33, the inflow port 6, and the like. Heat exchange (heat exchange) is performed with the high temperature exhaust gas flowing in each communication pipe 8 in contact with the communication pipe 8, the cleaning gas is warmed and dehumidified, and is discharged into the outside air from the outlet 7. .. Further, the water accumulated in the water tank 18 of the cleaning and dust collecting unit B is transferred into the processing tank 21 of the purification unit C via the drain pipe 30, and is automatically filtered and purified by the filter 25. Then, the purified water is pumped by the pump 32 through the water pipe 31 to the nozzle 27 of the cleaning and dust collecting unit B, and is repeatedly used for cleaning and dust collecting of the exhaust gas. Further, the filter 25 is properly removed and pulled up, and the mixed substances such as dust, dust, and impurities are discarded.

【0009】さらに洗浄集塵ユニットBにおけるノズル
27を、図1,図3に示すように、横型の分離タンク1
0の左右両側に夫々1個ずつ2個設け、一方を上向きの
斜後方向きに、また他方を下向きの斜後方向きにそれぞ
れすることによって、排気ガスと洗浄水とは図1に示す
ように分離タンク10内でよく混交して旋回流動し、洗
浄集塵効果が助勢される。
Further, as shown in FIGS. 1 and 3, the nozzle 27 in the cleaning and dust collecting unit B is replaced by a horizontal separation tank 1
The exhaust gas and the cleaning water are separated as shown in FIG. 1 by providing two ones on each of the left and right sides of 0, and by arranging one for the upward oblique rearward direction and the other for the downward oblique rearward direction. In the tank 10, they are well mixed and swirled to facilitate the cleaning and dust collecting effect.

【0010】なお図4に示した別の実施例では、前後に
排気ガスの吸込,排気口2,3を有するタンク1内の排
気ガス流路Sを囲繞して該排気ガスと熱授受を行う浄化
ガスの流入,出口6,7を有する熱交換器構成の排熱利
用除湿ユニットAと仕切遮板36で仕切られて下部室3
7下端がブロアー41を有する吸気口39にそして上部
室38上端が大気に開口する送気口40に夫々形成され
た冷却部ユニットDとが前後に隣接配設された構造のも
のが開示されている。なお42は、吸込口2に接続の吸
込管、43は焼却炉、44,45,46はダンパーであ
る。
In another embodiment shown in FIG. 4, exhaust gas is sucked in and out, and an exhaust gas flow path S in a tank 1 having exhaust ports 2 and 3 is surrounded to perform heat exchange with the exhaust gas. The lower chamber 3 is partitioned by the exhaust heat-dehumidifying unit A of the heat exchanger configuration having the purified gas inflow and outlets 6 and 7 and the partition shield plate 36.
7 is disclosed a structure in which a lower end of a cooling unit D formed at an intake port 39 having a blower 41 and an upper end of an upper chamber 38 at an air supply port 40 opening to the atmosphere are adjacently arranged in front and rear. There is. Incidentally, 42 is a suction pipe connected to the suction port 2, 43 is an incinerator, and 44, 45, 46 are dampers.

【0011】[0011]

【発明の効果】この発明装置は以上のようであって、自
動車の排気ガスなどのようにガス温度の高い有害ガスも
同時に除去、清浄化できると共に空気中に混在せる各種
粉塵,塵埃,夾雑物などを完全有効に除去集塵できる効
果がある。
As described above, the device of the present invention is capable of simultaneously removing and purifying harmful gases having a high gas temperature such as exhaust gas of automobiles and mixing various dusts, dusts and impurities in the air. It has the effect of completely removing dust and the like.

【0012】またこの発明では排気ガス洗浄集塵のため
の洗浄水が浄化ユニットで濾過、清澄化して繰返し循環
使用するシステムとなっているので、ミスト除去器やあ
との厄介な排水処理が必要ないものであると共に特にこ
の発明では汚染排気ガスを洗浄,除塵,浄化処理した浄
化ガスを最後に排熱利用除湿ユニットにおいて排熱で暖
め、除湿して大気中に排出するものであるから、大気中
へのガス拡散が悪くなったり、環境の汚染濃度が高くな
ったりする問題が解消でき、かつメンテナンスの面でも
合理的で経済的であるなど多くの優れた効果がある。ま
た硫黄分を含有している燃料をボイラーなどで燃焼する
際の排ガスから硫黄酸化物SOχを吸収・除去する排煙
脱硫装置の機能も果すことができる。
Further, in the present invention, the cleaning water for exhaust gas cleaning dust collection is a system in which it is filtered and clarified by the purifying unit and repeatedly circulated for use, so that a mist remover and subsequent troublesome waste water treatment are not required. In particular, according to the present invention, since the purified gas obtained by cleaning, dedusting, and purifying the contaminated exhaust gas is finally warmed by exhaust heat in the dehumidifying unit utilizing exhaust heat, dehumidified, and discharged into the atmosphere, There are many excellent effects such as the problem that gas diffusion to the inside becomes worse and the pollution concentration of the environment becomes higher, and the maintenance is rational and economical. Further, it can also function as a flue gas desulfurization device that absorbs and removes sulfur oxide SO χ from exhaust gas when burning fuel containing sulfur in a boiler or the like.

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

【図1】本発明の実施例の縦断説明図である。FIG. 1 is a vertical cross-sectional explanatory view of an embodiment of the present invention.

【図2】本発明の別の実施例の縦断説明図である。FIG. 2 is a vertical cross-sectional explanatory view of another embodiment of the present invention.

【図3】本発明の実施例のノズル装着部の説明図であ
る。
FIG. 3 is an explanatory diagram of a nozzle mounting portion according to the embodiment of this invention.

【図4】本発明のさらに別の実施例の縦断説明図であ
る。
FIG. 4 is a vertical cross-sectional explanatory view of still another embodiment of the present invention.

【符号の説明】 1 タンク 2 吸込口 3 排気口 4 前部室 5 後部室 6 流入口 7 流出口 8 連通管 9 垂下板 10 分離タンク 11 入口 12 出口 13 後壁 14 後部室 15 遮壁板 16 寸断切欠堰板 17 通孔 18 水槽 19 排水口 20 ドレン抜き 21 処理タンク 22 通入口 23 通出口 24 掩蓋 25 濾過器 26 支板 27 ノズル 28 矢印方向 29 通気管 30 排水管 31 送水管 32 ポンプ 33 排気管 34 35 バッフル 36 仕切遮板 37 下部室 38 上部室 39 吸気口 40 送気口 41 ブロアー 42 吸込管 43 焼却炉 44 45 46 ダンパー 47 煙突 A 排熱利用除湿ユニット B 洗浄集塵ユニット C 浄化ユニット D 冷却部ユニット S 排気ガス流路[Explanation of symbols] 1 Tank 2 Suction port 3 Exhaust port 4 Front chamber 5 Rear chamber 6 Inlet 7 Outlet 8 Communication pipe 9 Hanging plate 10 Separation tank 11 Inlet 12 Outlet 13 Rear wall 14 Rear chamber 15 Barrier plate 16 Shredding Notch weir plate 17 Through hole 18 Water tank 19 Drain port 20 Drain drain 21 Processing tank 22 Through hole 23 Through outlet 24 Cover 25 Filter 26 Branch plate 27 Nozzle 28 Arrow direction 29 Vent pipe 30 Drain pipe 31 Water pipe 32 Pump 33 Exhaust pipe 34 35 Baffle 36 Partition shield 37 Lower chamber 38 Upper chamber 39 Air inlet 40 Air inlet 41 Blower 42 Suction pipe 43 Incinerator 44 45 46 Damper 47 Chimney A Dehumidification unit using exhaust heat B Cleaning dust collection unit C Purification unit D Cooling Unit S S Exhaust gas flow path

Claims (1)

【特許請求の範囲】[Claims] 前後に排気ガスの吸込、排気口を有するタンク内の排気
ガス流路を囲繞して該排気ガスと熱授受を行う浄化ガス
の流入,出口を有する熱交換器構成の排熱利用除湿ユニ
ットと、上記の排気口に連通する前部入口と後部出口を
有すると共に出口下方に水槽を備えた分離タンク内の内
壁に斜後方向きのノズルを設けてその後方の出口近傍に
先端に複数の寸断切欠堰板を有する遮壁板が設けられた
出口を排熱利用除湿ユニットの流入口に連通させてなる
洗浄集塵ユニットと、該洗浄集塵ユニットの水槽及びノ
ズルにポンプを介装して連通させた着脱自在の濾過器を
有する浄化ユニットとからなり、排気ガスの脱硫除塵を
行うことを特徴とする排気ガス脱硫除塵装置。
Intake of exhaust gas in front and rear, exhaust gas utilization dehumidification unit of heat exchanger configuration having an inflow and outflow of purified gas that surrounds an exhaust gas flow path in a tank having an exhaust port and exchanges heat with the exhaust gas, A nozzle facing obliquely rearward is provided on the inner wall of the separation tank having a front inlet and a rear outlet communicating with the above-mentioned exhaust port and having a water tank below the outlet, and a plurality of cutout weirs at the tip near the outlet behind the outlet. A cleaning dust collecting unit in which an outlet provided with a barrier plate having a plate is connected to an inlet of a dehumidifying unit utilizing exhaust heat, and a water tank and a nozzle of the cleaning dust collecting unit are connected to each other through a pump. An exhaust gas desulfurization / dust removal device comprising a purification unit having a detachable filter and performing desulfurization / dust removal of exhaust gas.
JP4084931A 1992-03-06 1992-03-06 Exhaust gas desulfurization dust removing device Pending JPH05245327A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4084931A JPH05245327A (en) 1992-03-06 1992-03-06 Exhaust gas desulfurization dust removing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4084931A JPH05245327A (en) 1992-03-06 1992-03-06 Exhaust gas desulfurization dust removing device

Publications (1)

Publication Number Publication Date
JPH05245327A true JPH05245327A (en) 1993-09-24

Family

ID=13844440

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4084931A Pending JPH05245327A (en) 1992-03-06 1992-03-06 Exhaust gas desulfurization dust removing device

Country Status (1)

Country Link
JP (1) JPH05245327A (en)

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CN102949925A (en) * 2012-10-26 2013-03-06 张宏生 Exhaust gas desulphurization and dust-removal device
WO2015083950A1 (en) * 2013-12-02 2015-06-11 주식회사 바우만 Dry desulfurization system using absorption type dehumidifier
CN105854464A (en) * 2016-05-25 2016-08-17 顾飞华 Environment-friendly soldering tin smoke absorbing and purifying equipment
CN105921480A (en) * 2016-07-04 2016-09-07 李丹 Environmentally friendly purifying device for fume hood
CN106823727A (en) * 2017-02-24 2017-06-13 宜兴市创新环保有限公司 A kind of greasy filth waste gas purification and residual heat using device
CN108619885A (en) * 2017-03-24 2018-10-09 中国石油化工股份有限公司 A kind of fume desulfurizing tower and flue gas ash removal, desulfurization and wastewater treatment method
CN111265981A (en) * 2020-03-10 2020-06-12 江苏峰业科技环保集团股份有限公司 Absorption type desulphurization flue gas dehumidification system and method
CN113230843A (en) * 2021-06-02 2021-08-10 齐明 Flue gas desulfurization dust collector

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100943442B1 (en) * 2009-03-12 2010-02-19 덕 용 김 Dehumidification installation of desulfuri zation equipment
CN102949925A (en) * 2012-10-26 2013-03-06 张宏生 Exhaust gas desulphurization and dust-removal device
CN102949925B (en) * 2012-10-26 2015-01-07 张宏生 Exhaust gas desulphurization and dust-removal device
WO2015083950A1 (en) * 2013-12-02 2015-06-11 주식회사 바우만 Dry desulfurization system using absorption type dehumidifier
CN105854464A (en) * 2016-05-25 2016-08-17 顾飞华 Environment-friendly soldering tin smoke absorbing and purifying equipment
CN105921480A (en) * 2016-07-04 2016-09-07 李丹 Environmentally friendly purifying device for fume hood
CN106823727A (en) * 2017-02-24 2017-06-13 宜兴市创新环保有限公司 A kind of greasy filth waste gas purification and residual heat using device
CN108619885A (en) * 2017-03-24 2018-10-09 中国石油化工股份有限公司 A kind of fume desulfurizing tower and flue gas ash removal, desulfurization and wastewater treatment method
CN108619885B (en) * 2017-03-24 2020-06-05 中国石油化工股份有限公司 Flue gas desulfurization tower and flue gas dedusting, desulfurization and wastewater treatment method
CN111265981A (en) * 2020-03-10 2020-06-12 江苏峰业科技环保集团股份有限公司 Absorption type desulphurization flue gas dehumidification system and method
CN113230843A (en) * 2021-06-02 2021-08-10 齐明 Flue gas desulfurization dust collector

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