CN102853435A - Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device - Google Patents
Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device Download PDFInfo
- Publication number
- CN102853435A CN102853435A CN2012103753761A CN201210375376A CN102853435A CN 102853435 A CN102853435 A CN 102853435A CN 2012103753761 A CN2012103753761 A CN 2012103753761A CN 201210375376 A CN201210375376 A CN 201210375376A CN 102853435 A CN102853435 A CN 102853435A
- Authority
- CN
- China
- Prior art keywords
- tower
- flue gas
- cooling water
- spray
- purifying
- 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
- 238000000746 purification Methods 0.000 title abstract description 48
- 238000001816 cooling Methods 0.000 title abstract description 4
- 239000000779 smoke Substances 0.000 title description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 72
- 239000003546 flue gas Substances 0.000 claims abstract description 72
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 45
- 230000023556 desulfurization Effects 0.000 claims abstract description 45
- 238000010791 quenching Methods 0.000 claims abstract description 45
- 239000007921 spray Substances 0.000 claims abstract description 41
- 230000000171 quenching effect Effects 0.000 claims abstract description 40
- 239000000498 cooling water Substances 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000007789 gas Substances 0.000 claims abstract description 12
- 230000003009 desulfurizing effect Effects 0.000 claims 12
- 239000003517 fume Substances 0.000 claims 6
- 239000003513 alkali Substances 0.000 claims 1
- 239000011229 interlayer Substances 0.000 claims 1
- 238000005507 spraying Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 239000002906 medical waste Substances 0.000 description 20
- 239000000428 dust Substances 0.000 description 8
- 238000004380 ashing Methods 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 239000002920 hazardous waste Substances 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
本发明涉及一种双塔式急冷、喷淋脱硫净化一体化烟气净化装置,包括烟气急冷塔、脱硫净化装置,其特征是烟气急冷塔及脱硫净化装置设置成包括烟气急冷塔、喷淋脱硫净化塔、冷却水箱及碱液箱的一体化装置;冷却水箱及碱液箱的顶部分别固定连接急冷塔和喷淋脱硫净化塔,烟气急冷塔塔体上部设置烟气进口及连通压缩气体及冷却水箱的冷却水的气液喷头、底部设置回水口,喷淋脱硫净化塔上部设置烟气出口及连通碱液箱碱液的喷淋头,在喷淋脱硫净化塔内底部设置螺旋导流器及回液口,烟气急冷塔底部通过连接烟道与螺旋导流器底部的烟气进口连通。本发明的有益效果是:结构紧凑、体小量轻,急冷、喷淋脱硫净化效果优良,实现了清洁生产。
The invention relates to a flue gas purification device integrated with double-tower quenching, spraying, desulfurization and purification, which includes a flue gas quenching tower and a desulfurization purification device, and is characterized in that the flue gas quenching tower and the desulfurization purification device are set to include a flue gas quenching tower, The integrated device of spray desulfurization purification tower, cooling water tank and lye tank; the tops of cooling water tank and lye tank are fixedly connected to the quench tower and spray desulfurization purification tower respectively, and the upper part of the flue gas quench tower body is provided with flue gas inlet and connection The gas-liquid nozzle for compressed gas and cooling water of the cooling water tank, and the bottom of the water return port are set. The upper part of the spray desulfurization purification tower is provided with a flue gas outlet and a spray head connected to the lye tank. The deflector and the liquid return port, and the bottom of the flue gas quenching tower communicate with the flue gas inlet at the bottom of the spiral deflector through the connecting flue. The beneficial effects of the invention are: compact structure, small body and light weight, excellent effects of rapid cooling and spraying desulfurization and purification, and clean production is realized.
Description
技术领域 technical field
本发明涉及医疗废物处理领域烟气急冷及脱硫净化装置,尤其涉及一种适用于车载小型医疗废物处理设施用的双塔式急冷、喷淋脱硫净化一体化烟气净化装置。The invention relates to a flue gas quenching and desulfurization purification device in the field of medical waste treatment, in particular to a twin-tower type quenching, spray desulfurization and purification integrated flue gas purification device suitable for vehicle-mounted small medical waste treatment facilities.
背景技术 Background technique
医疗废物是一种影响广泛、危害极大的特殊危险废弃物。在《国家危险废物目录》中排名首位。如果对其处理不当或任意丢弃、扩散到生活环境中,可导致病菌传播、疾病流行,对人民群众生命健康构成极大威胁。Medical waste is a special hazardous waste with wide influence and great harm. It ranks first in the National Catalog of Hazardous Wastes. If it is not handled properly or discarded arbitrarily and spreads into the living environment, it can lead to the spread of germs and epidemics, posing a great threat to the lives and health of the people.
目前在我国大中型城市内均设置了医疗废物集中处理的定点单位。然而,在县级以下地区,特别是广大农村地区的中小型医疗机构所产生的医疗废物,由于分布面广或地处偏远、产生量不大,运输成本较高,难以纳入到市级以上的集中收集处理的网络内,成为医疗废物处置的盲区。根据国家有关规定,在不具备集中处置医疗废物条件的农村地区,医疗卫生机构应当按照要求,自行就地处置其产生的医疗废物,能够焚烧的,及时焚烧,不能焚烧的,消毒后集中填埋。针对上述要求,近年来,医疗废物处理领域正在潜心研究车载式医疗废物灰化设施,以实现设施体小量轻并可依不同现场需要随时移动到位,进行小批量及时处理的便利、环保的处理方式。At present, designated units for centralized treatment of medical waste have been set up in large and medium-sized cities in my country. However, the medical waste produced by small and medium-sized medical institutions in areas below the county level, especially in the vast rural areas, is difficult to be included in the medical wastes above the city level due to the wide distribution or remote location, the small amount of production, and the high transportation costs. The centralized collection and processing network has become a blind spot for medical waste disposal. According to the relevant state regulations, in rural areas that do not have the conditions for centralized disposal of medical waste, medical and health institutions should dispose of the medical waste they generate on the spot according to the requirements. If they can be incinerated, they should be incinerated in time; . In response to the above requirements, in recent years, the field of medical waste treatment has been concentrating on the research of vehicle-mounted medical waste ashing facilities, so as to realize the convenient and environmentally friendly treatment of small batches and timely treatment of small batches. Way.
烟气冷却、脱硫净化是医疗废物灰化处理的重要工艺过程,但现有大型医疗废物处理系统由于处理烟气量大,烟气成分复杂,采用了烟气急冷塔及多级脱硫净化装置,形成布局分散、体积大、占地面积大,操作复杂的烟气净化系统。此外,脱硫净化采用了干法或半干法工艺,消耗大量脱氧剂,并产生大量脱硫废物,处理不当极易造成二次污染。以上缺陷均无法适用于车载式小型医疗废物灰化设施。如何实现装置小型化、便携化并能达到医疗废物灰化处理的工艺要求,防止二次污染,成为业界探索的问题。Flue gas cooling, desulfurization and purification are important processes in the ashing treatment of medical waste, but the existing large-scale medical waste treatment system uses a flue gas quenching tower and a multi-stage desulfurization purification device due to the large amount of flue gas to be processed and the complex composition of the flue gas. Form a flue gas purification system with scattered layout, large volume, large floor area and complex operation. In addition, the desulfurization purification adopts dry or semi-dry process, which consumes a large amount of deoxidizer and produces a large amount of desulfurization waste. Improper treatment can easily cause secondary pollution. Above defect all can't be applicable to vehicle-mounted small medical waste ashing facility. How to realize the miniaturization and portability of the device, meet the process requirements of ashing treatment of medical waste, and prevent secondary pollution has become a problem explored by the industry.
发明内容 Contents of the invention
本发明的主要目的在于针对上述问题,提供一种适用于车载式小型医疗废物处理设施的双塔式急冷、喷淋脱硫净化一体化烟气净化装置,并能达到医疗废物灰化处理的工艺要求,实现清洁生产。The main purpose of the present invention is to address the above problems, to provide a dual-tower type quenching, spray desulfurization and purification integrated flue gas purification device suitable for vehicle-mounted small medical waste treatment facilities, and can meet the technological requirements of ashing treatment of medical waste , to achieve clean production.
本发明解决其技术问题所采用的技术方案是:The technical solution adopted by the present invention to solve its technical problems is:
一种双塔式急冷、喷淋脱硫净化一体化烟气净化装置,包括烟气急冷塔、脱硫净化装置,其特征在于所述烟气急冷塔及脱硫净化装置设置成包括烟气急冷塔、喷淋脱硫净化塔、冷却水箱及碱液箱的一体化装置;在冷却水箱及碱液箱的顶部分别固定连接所述急冷塔和喷淋脱硫净化塔,烟气急冷塔塔体上部设置烟气进口及连通压缩气体及冷却水箱的冷却水的气液喷头、底部设置回水口,喷淋脱硫净化塔上部设置烟气出口及连通碱液箱碱液的喷淋头,在喷淋脱硫净化塔内底部设置形成旋流烟气的螺旋导流器及回液口,烟气急冷塔底部通过连接烟道与所述螺旋导流器底部的烟气进口连通。A double-tower type quenching, spraying desulfurization purification integrated flue gas purification device, including a flue gas quenching tower, a desulfurization purification device, characterized in that the flue gas quenching tower and desulfurization purification device are set to include a flue gas quenching tower, a spraying The integrated device of desulfurization purification tower, cooling water tank and lye tank; the quench tower and spray desulfurization purification tower are respectively fixedly connected to the top of the cooling water tank and lye tank, and the upper part of the flue gas quench tower body is provided with a flue gas inlet And the gas-liquid nozzle connected to the compressed gas and the cooling water of the cooling water tank, the bottom is provided with a return port, the upper part of the spray desulfurization purification tower is provided with a flue gas outlet and a spray head connected to the lye tank lye, at the bottom of the spray desulfurization purification tower A spiral deflector and a liquid return port for forming swirling flue gas are provided, and the bottom of the flue gas quenching tower communicates with the flue gas inlet at the bottom of the spiral deflector through a connecting flue.
所述螺旋导流器包括一顶面为封闭盖体底部敞开的圆筒,在筒体环周侧壁上与圆筒中心线平行均布设置若干纵贯筒体侧壁的条形排气口,在各条形排气口外侧筒壁上沿条形排气口设置倾斜导流片。The spiral deflector includes a cylinder whose top surface is a closed cover and the bottom is open, and a number of strip-shaped exhaust ports are arranged on the circumferential side wall of the cylinder parallel to the center line of the cylinder and evenly distributed across the side wall of the cylinder. , on the outer cylinder wall of each strip-shaped exhaust port, an inclined guide vane is arranged along the strip-shaped exhaust port.
所述倾斜导流片与过其与筒体侧壁连接部位的圆筒切面间的夹角θ为30°-70°。The included angle θ between the inclined baffle and the cylindrical section passing through the connecting portion of the inclined baffle and the side wall of the cylinder is 30°-70°.
所述圆筒顶面的封闭盖体为上表面上凸下表面下凸的夹层曲面盖体。The closed cover on the top surface of the cylinder is a sandwich curved cover with an upper surface convex and a lower surface convex downward.
在所述烟气急冷塔回水口和喷淋脱硫净化45塔的回液口分别通过管道经回水集尘网和回液集尘网连接冷却水箱及碱液箱。The water return port of the flue gas quenching tower and the liquid return port of the spray desulfurization purification 45 tower are respectively connected to the cooling water tank and the lye tank through the return water dust collection net and the liquid return dust collection net through pipelines.
本发明的有益效果是:提供出一种采用湿法工艺的双塔式急冷、喷淋脱硫净化一体化烟气净化装置,将烟气急冷塔、喷淋脱硫净化塔及冷却水箱及碱液箱集成为一体,与传统外连冷却水及碱液管道的结构相比,结构紧凑、体小量轻,便携性强且无脱硫废物,循环水无外排,实现了清洁生产,防止二次污染。急冷效果好,烟气由600℃降至200℃时间小于1秒,尤其喷淋脱硫净化塔中设置了螺旋导流器,提高了脱硫净化效果,脱硫效率大于89%。对于粒径<10μm的烟气除尘效率高于95%,排放烟气的二噁英类去除率大于96%,达到医疗废物灰化处理的工艺要求。The beneficial effects of the present invention are: to provide a double-tower quenching, spray desulfurization and purification integrated flue gas purification device using a wet process, the flue gas quenching tower, spray desulfurization purification tower, cooling water tank and lye tank Integrated into one, compared with the traditional external cooling water and lye pipeline structure, it has compact structure, small body and light weight, strong portability, no desulfurization waste, no external discharge of circulating water, realizing clean production and preventing secondary pollution . The rapid cooling effect is good, and the time for flue gas to drop from 600°C to 200°C is less than 1 second. In particular, the spiral deflector is installed in the spray desulfurization purification tower, which improves the desulfurization purification effect, and the desulfurization efficiency is greater than 89%. The dust removal efficiency of the flue gas with a particle size of <10 μm is higher than 95%, and the removal rate of dioxins in the flue gas is higher than 96%, which meets the technological requirements for ashing treatment of medical waste.
附图说明 Description of drawings
图1是本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2是图1中螺旋导流器的横截面图。Fig. 2 is a cross-sectional view of the helical deflector in Fig. 1 .
图中:1烟气急冷塔,11烟气进口,12回水口,13加水口,14加碱液口,2喷淋脱硫净化塔,21烟气出口,回液口22,3喷淋头,41-42水泵,5联体箱,51冷却水箱,52碱液箱,61-62集尘网,7连接烟道,8气液喷头,9螺旋导流器,91条形排气口,92倾斜导流片,10压缩机。In the figure: 1 flue gas quenching tower, 11 flue gas inlet, 12 water return port, 13 water adding port, 14 lye adding port, 2 spray desulfurization purification tower, 21 flue gas outlet,
以下结合附图和实施例对本发明详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings and embodiments.
具体实施方式 Detailed ways
图1~图2示出一种双塔式急冷、喷淋脱硫净化一体化烟气净化装置,包括烟气急冷塔、脱硫净化装置,其特征在于所述烟气急冷塔及脱硫净化装置设置成包括烟气急冷塔1、喷淋脱硫净化塔2、冷却水箱51及碱液箱52的一体化装置;冷却水箱51与碱液箱52固定连接形成联体箱5。在冷却水箱51及碱液箱52的顶部分别固定连接上述烟气急冷塔1和喷淋脱硫净化塔2,急冷塔塔体上部设置烟气进口11及连通压缩气体及冷却水的气液喷头8、底部设置回水口12。本例中,烟气进口11设置在烟气急冷塔塔体顶部,气液喷头8通过塔体侧壁设置在烟气急冷塔塔体上部,冷却水箱51中的冷却水通过水泵41输送给气液喷头8,压缩气体由压缩机10经气体管道提供给气液喷头8。Figures 1 to 2 show a double-tower quenching, spray desulfurization and purification integrated flue gas purification device, including a flue gas quenching tower and a desulfurization purification device, which are characterized in that the flue gas quenching tower and the desulfurization purification device are arranged as An integrated device including flue gas quenching tower 1 , spray
上述喷淋脱硫净化塔2的上部设置烟气出口21及连通碱液箱52碱液的喷淋头3。本例中,烟气出口21设置在喷淋脱硫净化塔塔体顶部,喷淋头3通过塔体侧壁设置在烟气急冷塔塔体上部,喷淋头3采用了市售螺旋喷头。在喷淋脱硫净化塔内底部设置形成旋流烟气的螺旋导流器9及回液口22,螺旋导流器9包括一顶面为封闭盖体底部敞开的圆筒,在筒体环周侧壁上与圆筒中心线平行均布设置若干纵贯筒体侧壁的条形排气口91,在各条形排气口外侧筒壁上沿条形排气口设置倾斜导流片92,如图2所示,倾斜导流片92与过其与筒体侧壁连接部位的圆筒切面间的夹角θ为30°-70°。烟气急冷塔底部通过连接烟道7与上述螺旋导流器9底部的烟气进口连通。通过螺旋导流器的条形排气口及倾斜导流片导流,使从螺旋导流器底部进入的烟气形成高速涡旋气流,可与自上而下的喷淋碱液充分接触,达到良好脱硫及除尘净化效果。尤其圆筒顶面的封闭盖体为上表面上凸下表面下凸的夹层曲面盖体。这样,在筒内可防止湍流形成,更有利于烟气的脱硫、净化。The upper part of the spray
为滤除烟尘,上述烟气急冷塔回水口12和喷淋脱硫净化塔的回液口22分别通过管道经回水集尘网61和回液集尘网62连接冷却水箱51及碱液箱52。In order to filter out smoke and dust, the
本发明在车载式小型医疗废物处理设施中应用时,医疗废物在快速灰化炉的一燃室燃烧产生的烟气进入二燃室,在二燃室温度可达850~900℃,烟气在二燃室内二次燃烧处理后,除去其中绝大部分有机气体,剩余高温烟气在系统引风负压作用下依次进入烟气急冷塔1和喷淋脱硫净化塔2,其中烟气急冷塔采用了市售高效雾化气液喷头,由于在气液喷头中通入的压缩空气与冷却水形成高速下行水雾,与下行烟气同向流动,充分接触,使高温烟气温度迅速下降。运行过程中,经急冷后的烟气进入碱液喷淋脱硫净化塔2,烟气除去大部分的酸性气体并进一步降温,经上述两塔处理后的烟气温度可降至100℃~150℃,达到急冷、喷淋脱硫净化工艺要求When the present invention is applied in a vehicle-mounted small-scale medical waste treatment facility, the flue gas produced by the combustion of medical waste in the first combustion chamber of the rapid ashing furnace enters the second combustion chamber, and the temperature in the second combustion chamber can reach 850-900°C, and the flue gas is in the second combustion chamber. After the secondary combustion treatment in the secondary combustion chamber, most of the organic gases are removed, and the remaining high-temperature flue gas enters the flue gas quenching tower 1 and the spray
以上所述,仅是本发明的优选实施例而已,并非对本发明的形状材料和结构作任何形式上的限制。凡是依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above descriptions are only preferred embodiments of the present invention, and do not impose any restrictions on the shape, material and structure of the present invention. All simple modifications, equivalent changes and modifications made to the above embodiments according to the technical essence of the present invention still fall within the scope of the technical solutions of the present invention.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103753761A CN102853435A (en) | 2012-09-29 | 2012-09-29 | Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012103753761A CN102853435A (en) | 2012-09-29 | 2012-09-29 | Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102853435A true CN102853435A (en) | 2013-01-02 |
Family
ID=47400256
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012103753761A Pending CN102853435A (en) | 2012-09-29 | 2012-09-29 | Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102853435A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105805764A (en) * | 2016-03-14 | 2016-07-27 | 江正云 | Medical waste incineration technological method |
CN107469586A (en) * | 2017-09-29 | 2017-12-15 | 广东省环境科学研究院 | A kind of plasma organic exhaust gas purifying system integrated with biofilter and method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2401791Y (en) * | 1999-12-30 | 2000-10-18 | 山东工业大学热能与环保工程技术研究中心 | Flue gas purifier with prepositioned spraying swirl cylinder water membrane purifying |
CN200998640Y (en) * | 2007-01-30 | 2008-01-02 | 袁少峰 | Garbage disposal bitubular dust cleaner |
JP4524270B2 (en) * | 2006-07-10 | 2010-08-11 | 三菱重工環境・化学エンジニアリング株式会社 | Exhaust gas cooling facility and control method thereof |
CN101988531A (en) * | 2010-08-12 | 2011-03-23 | 苏州顶裕节能设备有限公司 | Air inlet vortex generating device of industrial tower |
CN202070282U (en) * | 2011-05-19 | 2011-12-14 | 山东昭和新材料科技股份有限公司 | Dry emergency absorption system of aluminum fluoride |
CN202844856U (en) * | 2012-09-29 | 2013-04-03 | 天津市环境保护科学研究院 | Double-tower type quenching and spraying desulfuration and purification integrated smoke purification device |
-
2012
- 2012-09-29 CN CN2012103753761A patent/CN102853435A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2401791Y (en) * | 1999-12-30 | 2000-10-18 | 山东工业大学热能与环保工程技术研究中心 | Flue gas purifier with prepositioned spraying swirl cylinder water membrane purifying |
JP4524270B2 (en) * | 2006-07-10 | 2010-08-11 | 三菱重工環境・化学エンジニアリング株式会社 | Exhaust gas cooling facility and control method thereof |
CN200998640Y (en) * | 2007-01-30 | 2008-01-02 | 袁少峰 | Garbage disposal bitubular dust cleaner |
CN101988531A (en) * | 2010-08-12 | 2011-03-23 | 苏州顶裕节能设备有限公司 | Air inlet vortex generating device of industrial tower |
CN202070282U (en) * | 2011-05-19 | 2011-12-14 | 山东昭和新材料科技股份有限公司 | Dry emergency absorption system of aluminum fluoride |
CN202844856U (en) * | 2012-09-29 | 2013-04-03 | 天津市环境保护科学研究院 | Double-tower type quenching and spraying desulfuration and purification integrated smoke purification device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105805764A (en) * | 2016-03-14 | 2016-07-27 | 江正云 | Medical waste incineration technological method |
CN107469586A (en) * | 2017-09-29 | 2017-12-15 | 广东省环境科学研究院 | A kind of plasma organic exhaust gas purifying system integrated with biofilter and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101799169B (en) | A device that guides the airflow to impact the liquid surface tangentially to form a wet airflow | |
CN203494388U (en) | Flue gas desulfurization and dedusting device of coal-fired boiler | |
CN204502786U (en) | A kind of novel ultra-clean desulfurizer | |
CN202844856U (en) | Double-tower type quenching and spraying desulfuration and purification integrated smoke purification device | |
CN214513698U (en) | Domestic waste pyrolysis oven dust removal sweetener | |
CN203678203U (en) | Tristate purifier | |
CN205796820U (en) | A kind of desulfurating dust-removing equipment | |
CN102853435A (en) | Dual-tower shock-cooling and sprinkling desulphurization purification integrated smoke purifying device | |
CN106466544A (en) | The cleaning system of dusty gas | |
CN201880472U (en) | Flue gas desulfurizing and dedusting device for industrial coal-fired boiler | |
CN201609640U (en) | Tail water body structure for guiding airflow to tangentially impact liquid level to form moist airflow | |
CN104492209A (en) | Petroleum ether exhaust-gas dedusting and recovery device | |
CN204294087U (en) | Exhaust processor | |
CN207856592U (en) | A kind of sugaring workshop boiler waste gas treating device | |
CN106964246A (en) | A kind of flue gas processing device | |
CN207871891U (en) | High-efficient desulfurizing tower | |
CN205598924U (en) | Novel industrial waste gas multi -stage purification device | |
CN209406039U (en) | A kind of deacidification device for clearing up room | |
CN207356875U (en) | A kind of Novel desulfurization tower | |
CN206688441U (en) | A swirling spray tower | |
CN204502779U (en) | A kind of anticlogging three-phase turbulent current barrel high-efficient desulfation dust-extraction device | |
CN221933499U (en) | A tail gas absorption tower with high content of particulate matter | |
CN201249087Y (en) | Double subtraction energy saving and emission reduction environmental protection complete equipment | |
CN204601932U (en) | A kind of numb stone water bath dust-removing desulphurization system containing double-stage desulfurizing tower | |
CN204799092U (en) | Set up glass fiber stove waste gas desulphurization unit of turbocharged torrent ware |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130102 |