CN216498444U - Integrated wet waste gas purification system - Google Patents

Integrated wet waste gas purification system Download PDF

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CN216498444U
CN216498444U CN202122907920.XU CN202122907920U CN216498444U CN 216498444 U CN216498444 U CN 216498444U CN 202122907920 U CN202122907920 U CN 202122907920U CN 216498444 U CN216498444 U CN 216498444U
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tower
gas purification
waste gas
air
pipe
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矫锋
苏杭
于文斌
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Lvshui Qingshan Environmental Protection Technology Dalian Co ltd
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Lvshui Qingshan Environmental Protection Technology Dalian Co ltd
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Abstract

The utility model discloses an integrated wet waste gas purification system which comprises a dust removal tower, wherein the right end of a blower is connected with the waste gas purification tower through a fourth gas pipe and a third gas inlet, a plurality of gas risers are arranged at the top ends of a first tower plate and a second tower plate in a staggered mode, bubble caps are arranged at the top ends of the gas risers, overflow weirs are arranged at one end of the inner side of the second tower plate, and one ends of the outer sides of a liquid return pipe and a liquid inlet pipe are fixedly connected to the upper side and the lower side of one end of the inner side of an absorption liquid circulating device respectively. In the utility model, the first tower plate, the second tower plate, the overflow weir, the gas rising pipe, the bubble cap, the liquid inlet pipe, the liquid return pipe and the absorption liquid circulating device are mutually matched to form a system utilizing the wet-method full-component waste gas purification method, the waste gas treatment efficiency is improved, corresponding components in the waste gas are absorbed by the absorption liquid on each layer of tower plate, and the device has the advantages of wide application range, small occupied space and good purification effect, and is suitable for purification treatment of various waste gases.

Description

一种一体化湿法废气净化系统An integrated wet exhaust gas purification system

技术领域technical field

本实用新型涉及废气处理领域,尤其涉及一种一体化湿法废气净化系统。The utility model relates to the field of waste gas treatment, in particular to an integrated wet waste gas purification system.

背景技术Background technique

大气污染物是指由于人类活动或自然过程排入大气的并对人类或环境产生的有害影响的那些物质,大气污染物的种类很多,根据其存在的特征可分为气溶胶污染物和气态污染物两类,气溶胶污染物是指空气中的固体粒子和液体粒子,或固体和液体粒子在气体介质中的悬浮体,大气中的气态污染物是以分子状态存在的,气态污染物的种类很多,大部分为无机气体,常见的有以二氧化硫为主的含硫化合物,以一氧化氮和二氧化氮为主的台氮化合物;以一氧化碳、二氧化碳为主的碳的氧化物;以烷烃、烯烃和芳香烃类为主的碳氢化合物,以氟化氢、氯化氢为主的卤素化合物,大到影响全球的温室效应、臭氧层破坏,小到个别地区的酸雨、光化学污染等各种影响人类生活健康的问题都是由气态污染造成的。Air pollutants refer to those substances that are discharged into the atmosphere due to human activities or natural processes and have harmful effects on humans or the environment. There are many types of air pollutants, which can be divided into aerosol pollutants and gaseous pollutants according to their characteristics. There are two types of pollutants. Aerosol pollutants refer to solid particles and liquid particles in the air, or suspensions of solid and liquid particles in gaseous media. Gaseous pollutants in the atmosphere exist in a molecular state. The types of gaseous pollutants There are many, most of which are inorganic gases. The common ones are sulfur-containing compounds mainly composed of sulfur dioxide, nitrogen compounds mainly composed of nitric oxide and nitrogen dioxide; carbon oxides mainly composed of carbon monoxide and carbon dioxide; Hydrocarbons dominated by olefins and aromatic hydrocarbons, halogen compounds dominated by hydrogen fluoride and hydrogen chloride, which can affect the global greenhouse effect and ozone layer destruction, as small as acid rain and photochemical pollution in individual regions. The problems are all caused by gaseous pollution.

针对气溶胶污染物的处理主要以除尘为主,包括喷淋除尘、重力沉降、旋风除尘、电除尘、布袋除尘等各种方法,针对气态污染物因成分不同应采用不同的方法,处理二氧化硫主要采用氧化钙吸收,根据使用氧化钙状态的不同又分为干法、半干法、湿法脱硫三种;处理氮氧化物主要采用还原燃烧和化学吸收,处理氟化氢等卤素化合物主要采用活性炭吸附和化学吸收,由于实际生产中产生的废气成分复杂,往往粉尘、飞灰、氮氧化物、硫化物、卤化物等各种污染物需处理,需将各种对应的处理装置组合使用才能达到标准排放。The treatment of aerosol pollutants is mainly based on dust removal, including spray dust removal, gravity sedimentation, cyclone dust removal, electrostatic dust removal, bag dust removal and other methods. Different methods should be used for gaseous pollutants due to different components. Calcium oxide is used for absorption, which can be divided into dry, semi-dry and wet desulfurization according to the different states of calcium oxide; nitrogen oxides are mainly treated by reducing combustion and chemical absorption, and halogen compounds such as hydrogen fluoride are mainly treated by activated carbon adsorption and desulphurization. Chemical absorption, due to the complex composition of waste gas generated in actual production, often dust, fly ash, nitrogen oxides, sulfides, halides and other pollutants need to be treated, and various corresponding treatment devices need to be used in combination to achieve standard emissions. .

实用新型内容Utility model content

本实用新型的目的是为了解决现有技术中存在的缺点,而提出的一种一体化湿法废气净化系统。The purpose of the utility model is to propose an integrated wet waste gas purification system in order to solve the shortcomings existing in the prior art.

为了实现上述目的,本实用新型采用了如下技术方案:一种一体化湿法废气净化系统,包括除尘塔,所述除尘塔左端顶部设置有水管,所述水管左端固定连接有喷淋循环装置,所述除尘塔顶端中部设置有第一出气口,所述第一出气口顶端通过第一气管连接有鼓风机,所述鼓风机右端通过第四气管和第三进气口连接有废气净化塔,所述废气净化塔内壁固定连接有多个第一塔板,所述废气净化塔内壁在第一塔板之间固定连接有第二塔板,所述第一塔板和第二塔板顶端交错设置有多个升气管,所述升气管顶端均设置有泡罩,所述第二塔板内侧一端均设置有溢流堰,所述废气净化塔靠近第一塔板上侧均设置有回液管,所述废气净化塔靠近第二塔板上侧均设置有进液管,所述回液管和进液管外侧一端分别固定连接在吸收液循环装置内侧一端的上下两侧,所述废气净化塔顶端设置有第二出气口,所述第二出气口顶端通过第二气管和第二进气口连接有活性炭吸附器,所述活性炭吸附器顶端中部设置有第三出气口,所述第三出气口顶端通过第三气管连接有引风机,所述活性炭吸附器前端中部固定连接有控制器。In order to achieve the above purpose, the utility model adopts the following technical scheme: an integrated wet waste gas purification system, comprising a dust removal tower, a water pipe is arranged on the top of the left end of the dust removal tower, and a spray circulation device is fixedly connected to the left end of the water pipe, A first air outlet is arranged in the middle of the top of the dust removal tower, the top of the first air outlet is connected with a blower through a first air pipe, and the right end of the blower is connected with an exhaust gas purification tower through a fourth air pipe and a third air inlet. The inner wall of the exhaust gas purification tower is fixedly connected with a plurality of first trays, the inner wall of the exhaust gas purification tower is fixedly connected with a second tray between the first trays, and the tops of the first tray and the second tray are staggered. a plurality of gas risers, the tops of the gas risers are all provided with bubble caps, one end of the inner side of the second tray is provided with an overflow weir, and the waste gas purification tower is provided with a liquid return pipe on the upper side near the first tray, The waste gas purification tower is provided with a liquid inlet pipe on the upper side near the second tray, and the liquid return pipe and the outer end of the liquid inlet pipe are fixedly connected to the upper and lower sides of the inner end of the absorption liquid circulation device, respectively. The waste gas purification tower The top is provided with a second air outlet, the top of the second air outlet is connected with an activated carbon adsorber through the second air pipe and the second air inlet, and a third air outlet is arranged in the middle of the top of the activated carbon adsorber. The top of the air port is connected with an induced draft fan through a third air pipe, and a controller is fixedly connected to the middle of the front end of the activated carbon adsorber.

作为上述技术方案的进一步描述:As a further description of the above technical solutions:

所述第三进气口右端设置在废气净化塔左端。The right end of the third air inlet is arranged at the left end of the exhaust gas purification tower.

作为上述技术方案的进一步描述:As a further description of the above technical solutions:

所述第二进气口右端设置在活性炭吸附器左端。The right end of the second air inlet is arranged at the left end of the activated carbon adsorber.

作为上述技术方案的进一步描述:As a further description of the above technical solution:

所述第一出气口、第二出气口和第三出气口内径顶部均设置有除沫装置。The top of the inner diameter of the first air outlet, the second air outlet and the third air outlet are all provided with a defoaming device.

作为上述技术方案的进一步描述:As a further description of the above technical solutions:

所述水管底端右侧均匀设置有多个喷头。A plurality of spray heads are evenly arranged on the right side of the bottom end of the water pipe.

作为上述技术方案的进一步描述:As a further description of the above technical solution:

所述除尘塔左端中部设置有第一进气口。The middle part of the left end of the dust removal tower is provided with a first air inlet.

作为上述技术方案的进一步描述:As a further description of the above technical solutions:

所述引风机右端通过管道连接有排气筒。The right end of the induced draft fan is connected with an exhaust cylinder through a pipeline.

作为上述技术方案的进一步描述:As a further description of the above technical solutions:

所述喷淋循环装置、鼓风机、吸收液循环装置和引风机均与控制器电性连接。The spray circulation device, the blower, the absorption liquid circulation device and the induced draft fan are all electrically connected with the controller.

本实用新型具有如下有益效果:The utility model has the following beneficial effects:

本实用新型中,废气通过第一进气口进入除尘塔,经过喷淋循环装置、水管和喷头除尘后利用鼓风机送入废气净化塔,在废气净化塔内废气自下而上逐层通过多个塔板,而通过第一塔板、第二塔板、溢流堰、升气管、泡罩、进液管、回液管和吸收液循环装置相互配合,组成一个利用湿法全组分废气净化方法的系统,既方便后期维修,也提高了废气处理效率,有利于吸收塔的标准化、模块化,废气内相应成分被各层塔板上的吸收液吸收,净化后的气体从废气净化塔顶部排出进入活性炭吸附器,活性炭吸附器将废气中残留污染物吸收,处理后废气达到排放标准经排气筒排放,此装置适用范围广、占地空间小、净化效果好,适用于各种废气的净化处理。In the utility model, the waste gas enters the dust removal tower through the first air inlet, and is sent to the waste gas purification tower by the blower after being dedusted by the spray circulation device, the water pipe and the nozzle. The first plate, the second plate, the overflow weir, the gas riser, the bubble cap, the liquid inlet pipe, the liquid return pipe and the absorption liquid circulation device cooperate with each other to form a whole-component waste gas purification using the wet method. The system of the method is not only convenient for later maintenance, but also improves the efficiency of waste gas treatment, which is conducive to the standardization and modularization of the absorption tower. It is discharged into the activated carbon adsorber. The activated carbon adsorber absorbs the residual pollutants in the exhaust gas. After the treatment, the exhaust gas reaches the emission standard and is discharged through the exhaust pipe. This device has a wide range of applications, small footprint and good purification effect. Purification treatment.

附图说明Description of drawings

图1为本实用新型提出的一种一体化湿法废气净化系统的结构示意图;Fig. 1 is the structural representation of a kind of integrated wet waste gas purification system proposed by the utility model;

图2为图1中A处放大图;Fig. 2 is an enlarged view at A in Fig. 1;

图3为图2中B处放大图。FIG. 3 is an enlarged view of B in FIG. 2 .

图例说明:illustration:

1、除尘塔;2、第一进气口;3、喷淋循环装置;4、第一出气口;5、除沫装置;6、第一气管;7、吸收液循环装置;8、回液管;9、进液管;10、第一塔板;11、升气管;12、第二出气口;13、第二塔板;14、第二气管; 15、第三出气口;16、第三气管;17、排气筒;18、引风机;19、控制器; 20、活性炭吸附器;21、第二进气口;22、废气净化塔;23、第三进气口; 24、第四气管;25、鼓风机;26、水管;27、喷头;28、泡罩;29、溢流堰。1. Dust removal tower; 2. The first air inlet; 3. The spraying circulation device; 4. The first air outlet; 5. The defoaming device; 6. The first gas pipe; pipe; 9, liquid inlet pipe; 10, the first tray; 11, gas riser; 12, the second gas outlet; 13, the second tray; 14, the second gas pipe; 15, the third gas outlet; 16, the first Three air pipes; 17, exhaust pipe; 18, induced draft fan; 19, controller; 20, activated carbon adsorber; 21, the second air inlet; 22, exhaust gas purification tower; 23, the third air inlet; 24, the first Four air pipes; 25, blower; 26, water pipe; 27, nozzle; 28, bubble cap; 29, overflow weir.

具体实施方式Detailed ways

下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, rather than all the implementations. example. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.

在本实用新型的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制;术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性,此外,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本实用新型中的具体含义。In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner" and "outer" The orientation or positional relationship indicated by etc. is based on the orientation or positional relationship shown in the accompanying drawings, which is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, with a specific orientation. Therefore, it should not be construed as a limitation to the present invention; the terms "first", "second" and "third" are only used for descriptive purposes, and should not be construed as indicating or implying relative importance. In addition, Unless otherwise expressly specified and limited, the terms "installed", "connected" and "connected" should be understood in a broad sense, for example, it may be a fixed connection, a detachable connection, or an integral connection; it may be a mechanical connection, It can also be an electrical connection; it can be a direct connection, an indirect connection through an intermediate medium, or an internal connection between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations.

参照图1-3,本实用新型提供的一种实施例:一种一体化湿法废气净化系统,包括除尘塔1,除尘塔1左端顶部设置有水管26,水管26左端固定连接有喷淋循环装置3,进行废气除尘,除尘塔1顶端中部设置有第一出气口4,第一出气口4顶端通过第一气管6连接有鼓风机25,鼓风机25右端通过第四气管24和第三进气口23连接有废气净化塔22,将废气送入废气净化塔22中,废气净化塔22内壁固定连接有多个第一塔板10,废气净化塔22内壁在第一塔板10之间固定连接有第二塔板13,第一塔板10和第二塔板13顶端交错设置有多个升气管11,升气管11顶端均设置有泡罩28,第二塔板13内侧一端均设置有溢流堰29,塔体内的N层塔板,第N层塔板外径与塔体内径相配合,实现塔体径向封堵,第N-1层塔板与塔体内壁间形成溢流口,废气净化塔22 靠近第一塔板10上侧均设置有回液管8,废气净化塔22靠近第二塔板13上侧均设置有进液管9,回液管8和进液管9外侧一端分别固定连接在吸收液循环装置7内侧一端的上下两侧,组成一个利用湿法全组分废气净化方法的系统,既方便后期维修,也提高了废气处理效率,有利于吸收塔的标准化、模块化,废气净化塔22顶端设置有第二出气口12,第二出气口12顶端通过第二气管14和第二进气口21连接有活性炭吸附器20,活性炭吸附器20顶端中部设置有第三出气口15,第三出气口15顶端通过第三气管16连接有引风机 18,排出净化好的废气,活性炭吸附器20前端中部固定连接有控制器19,废气通过第一进气口2进入除尘塔1,经过喷淋循环装置3、水管26和喷头27 除尘后利用鼓风机25送入废气净化塔22,在废气净化塔22内废气自下而上逐层通过多个塔板,而通过第一塔板10、第二塔板13、溢流堰29、升气管 11、泡罩28、进液管9、回液管8和吸收液循环装置7相互配合,组成一个利用湿法全组分废气净化方法的系统,既方便后期维修,也提高了废气处理效率,有利于吸收塔的标准化、模块化,废气内相应成分被各层塔板上的吸收液吸收,净化后的气体从废气净化塔22顶部排出进入活性炭吸附器20,活性炭吸附器20将废气中残留污染物吸收,处理后废气达到排放标准经排气筒 17排放,此装置适用范围广、占地空间小、净化效果好,适用于各种废气的净化处理。1-3, an embodiment provided by the present utility model: an integrated wet waste gas purification system, including a dust removal tower 1, the top of the left end of the dust removal tower 1 is provided with a water pipe 26, and the left end of the water pipe 26 is fixedly connected with a spray circulation The device 3 is used to dedust the exhaust gas. A first air outlet 4 is provided in the middle of the top of the dust removal tower 1. The top of the first air outlet 4 is connected with a blower 25 through the first air pipe 6. The right end of the blower 25 passes through the fourth air pipe 24 and the third air inlet. 23 is connected with a waste gas purification tower 22, and the waste gas is sent into the waste gas purification tower 22, the inner wall of the waste gas purification tower 22 is fixedly connected with a plurality of first trays 10, and the inner wall of the exhaust gas purification tower 22 is fixedly connected between the first trays 10. The top of the second tray 13, the first tray 10 and the second tray 13 are alternately provided with a plurality of gas risers 11, the top of the gas risers 11 are all provided with a bubble cap 28, and one end of the inner side of the second tray 13 is provided with an overflow Weir 29, the N-layer column plate in the tower body, the outer diameter of the N-th layer column plate is matched with the inner diameter of the column body to realize radial sealing of the column body, and an overflow port is formed between the N-1 layer column plate and the inner wall of the column, The waste gas purification tower 22 is provided with a liquid return pipe 8 near the upper side of the first tray 10, and the waste gas purification tower 22 is provided with a liquid inlet pipe 9 near the upper side of the second tray 13. The liquid return pipe 8 and the outside of the liquid inlet pipe 9 One end is fixedly connected to the upper and lower sides of the inner end of the absorption liquid circulation device 7 to form a system using the wet method of full-component exhaust gas purification method, which is convenient for later maintenance and improves the efficiency of exhaust gas treatment, which is conducive to the standardization of the absorption tower. Modularized, the top of the exhaust gas purification tower 22 is provided with a second air outlet 12, the top of the second air outlet 12 is connected with an activated carbon adsorber 20 through the second air pipe 14 and the second air inlet 21, and the middle of the top of the activated carbon adsorber 20 is provided. Three air outlets 15, the top of the third air outlet 15 is connected with an induced draft fan 18 through the third air pipe 16 to discharge the purified exhaust gas, and a controller 19 is fixedly connected to the middle of the front end of the activated carbon adsorber 20, and the exhaust gas enters through the first air inlet 2. The dust removal tower 1 is sent to the waste gas purification tower 22 by the blower 25 after the dust is removed by the spray circulation device 3, the water pipe 26 and the nozzle 27. The first tray 10, the second tray 13, the overflow weir 29, the gas riser 11, the bubble cap 28, the liquid inlet pipe 9, the liquid return pipe 8 and the absorption liquid circulation device 7 cooperate with each other to form a full-component wet method. The system of waste gas purification method not only facilitates post-maintenance, but also improves the efficiency of waste gas treatment, which is conducive to the standardization and modularization of absorption towers. The top of the tower 22 is discharged into the activated carbon adsorber 20, and the activated carbon adsorber 20 absorbs the residual pollutants in the exhaust gas. After the treatment, the exhaust gas reaches the emission standard and is discharged through the exhaust pipe 17. This device has a wide range of applications, small footprint and good purification effect. It is suitable for the purification treatment of various exhaust gases.

第三进气口23右端设置在废气净化塔22左端,第二进气口21右端设置在活性炭吸附器20左端,便于废气的进入,第一出气口4、第二出气口12和第三出气口15内径顶部均设置有除沫装置5,防止吸收液和喷淋液中水分被废气带出,造成烟道管路的腐蚀和阻塞,水管26底端右侧均匀设置有多个喷头27,进行除尘,除尘塔1左端中部设置有第一进气口2,废气进入除尘塔1 中,引风机18右端通过管道连接有排气筒17,排出净化好的气体,喷淋循环装置3、鼓风机25、吸收液循环装置7和引风机18均与控制器19电性连接,控制装置正常运行。The right end of the third air inlet 23 is arranged at the left end of the exhaust gas purification tower 22, and the right end of the second air inlet 21 is arranged at the left end of the activated carbon adsorber 20 to facilitate the entry of waste gas. The first air outlet 4, the second air outlet 12 and the third outlet The top of the inner diameter of the air port 15 is provided with a de-foaming device 5 to prevent the moisture in the absorption liquid and the spray liquid from being carried out by the exhaust gas, causing corrosion and blockage of the flue pipeline. For dust removal, a first air inlet 2 is arranged in the middle of the left end of the dust removal tower 1, the exhaust gas enters the dust removal tower 1, the right end of the induced draft fan 18 is connected with an exhaust pipe 17 through a pipeline, and the purified gas is discharged. The spray circulation device 3, the blower 25. Both the absorption liquid circulation device 7 and the induced draft fan 18 are electrically connected to the controller 19, and the control device operates normally.

工作原理:废气通过第一进气口2进入除尘塔1,经过喷淋循环装置3、水管26和喷头27除尘后利用鼓风机25送入废气净化塔22,在废气净化塔 22内废气自下而上逐层通过多个塔板,而通过第一塔板10、第二塔板13、溢流堰29、升气管11、泡罩28、进液管9、回液管8和吸收液循环装置7相互配合,组成一个利用湿法全组分废气净化方法的系统,既方便后期维修,也提高了废气处理效率,有利于吸收塔的标准化、模块化,废气内相应成分被各层塔板上的吸收液吸收,净化后的气体从废气净化塔22顶部排出进入活性炭吸附器20,活性炭吸附器20将废气中残留污染物吸收,处理后废气达到排放标准经排气筒17排放,此装置适用范围广、占地空间小、净化效果好,适用于各种废气的净化处理。Working principle: the exhaust gas enters the dust removal tower 1 through the first air inlet 2, passes through the spray circulation device 3, the water pipe 26 and the nozzle 27 for dust removal, and then is sent to the exhaust gas purification tower 22 by the blower 25. The upper layer passes through a plurality of trays, and passes through the first tray 10, the second tray 13, the overflow weir 29, the gas riser 11, the bubble cap 28, the liquid inlet pipe 9, the liquid return pipe 8 and the absorption liquid circulation device 7. Cooperate with each other to form a system that utilizes the wet full-component exhaust gas purification method, which not only facilitates later maintenance, but also improves the efficiency of exhaust gas treatment, which is conducive to the standardization and modularization of the absorption tower. The absorbing liquid is absorbed, and the purified gas is discharged from the top of the exhaust gas purification tower 22 into the activated carbon adsorber 20. The activated carbon adsorber 20 absorbs the residual pollutants in the exhaust gas, and the treated exhaust gas reaches the emission standard and is discharged through the exhaust pipe 17. This device is suitable for It has a wide range, small footprint and good purification effect, and is suitable for the purification treatment of various waste gases.

最后应说明的是:以上所述仅为本实用新型的优选实施例而已,并不用于限制本实用新型,尽管参照前述实施例对本实用新型进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换,凡在本实用新型的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。Finally, it should be noted that the above are only the preferred embodiments of the present invention, and are not intended to limit the present invention. , it can still modify the technical solutions recorded in the foregoing embodiments, or perform equivalent replacements to some of the technical features. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model, All should be included within the protection scope of the present invention.

Claims (8)

1. The utility model provides an integration wet process exhaust gas purification system, includes gas wash tower (1), its characterized in that: the top of the left end of the dust removing tower (1) is provided with a water pipe (26), the left end of the water pipe (26) is fixedly connected with a spraying circulating device (3), the middle part of the top end of the dust removing tower (1) is provided with a first air outlet (4), the top end of the first air outlet (4) is connected with an air blower (25) through a first air pipe (6), the right end of the air blower (25) is connected with a waste gas purification tower (22) through a fourth air pipe (24) and a third air inlet (23), the inner wall of the waste gas purification tower (22) is fixedly connected with a plurality of first tower plates (10), the inner wall of the waste gas purification tower (22) is fixedly connected with second tower plates (13) between the first tower plates (10), the top ends of the first tower plates (10) and the second tower plates (13) are provided with a plurality of air risers (11) in a staggered manner, the top ends of the air risers (11) are provided with bubble caps (28), one end of the inner side of each second tower plate (13) is provided with an overflow weir (29), the waste gas purification tower (22) is provided with a liquid return pipe (8) close to the upper side of the first tower plate (10), the waste gas purification tower (22) is provided with a liquid inlet pipe (9) close to the upper side of the second tower plate (13), the outer ends of the liquid return pipe (8) and the liquid inlet pipe (9) are respectively and fixedly connected with the upper side and the lower side of one end of the inner side of the absorption liquid circulating device (7), a second air outlet (12) is arranged at the top end of the waste gas purification tower (22), the top end of the second air outlet (12) is connected with an activated carbon adsorber (20) through a second air pipe (14) and a second air inlet (21), a third air outlet (15) is arranged in the middle of the top end of the activated carbon absorber (20), the top end of the third air outlet (15) is connected with a draught fan (18) through a third air pipe (16), the middle part of the front end of the activated carbon adsorber (20) is fixedly connected with a controller (19).
2. An integrated wet flue gas purification system according to claim 1, wherein: the right end of the third air inlet (23) is arranged at the left end of the waste gas purification tower (22).
3. An integrated wet flue gas purification system according to claim 1, wherein: the right end of the second air inlet (21) is arranged at the left end of the activated carbon absorber (20).
4. An integrated wet flue gas purification system according to claim 1, wherein: and the inner diameter tops of the first air outlet (4), the second air outlet (12) and the third air outlet (15) are all provided with a defoaming device (5).
5. An integrated wet flue gas purification system according to claim 1, wherein: a plurality of spray heads (27) are uniformly arranged on the right side of the bottom end of the water pipe (26).
6. An integrated wet flue gas purification system according to claim 1, wherein: the middle part of the left end of the dust removing tower (1) is provided with a first air inlet (2).
7. An integrated wet flue gas purification system according to claim 1, wherein: the right end of the induced draft fan (18) is connected with an exhaust funnel (17) through a pipeline.
8. An integrated wet exhaust gas purification system according to claim 1, wherein: the spraying circulating device (3), the air blower (25), the absorption liquid circulating device (7) and the induced draft fan (18) are all electrically connected with the controller (19).
CN202122907920.XU 2021-11-25 2021-11-25 Integrated wet waste gas purification system Active CN216498444U (en)

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