CN101721901A - Flue gas desulfurization and denitration purifying device in chimney of horizontal flue - Google Patents
Flue gas desulfurization and denitration purifying device in chimney of horizontal flue Download PDFInfo
- Publication number
- CN101721901A CN101721901A CN201010031308A CN201010031308A CN101721901A CN 101721901 A CN101721901 A CN 101721901A CN 201010031308 A CN201010031308 A CN 201010031308A CN 201010031308 A CN201010031308 A CN 201010031308A CN 101721901 A CN101721901 A CN 101721901A
- Authority
- CN
- China
- Prior art keywords
- chimney
- flue
- sieve plate
- flue gas
- purification
- 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
- 239000003546 flue gas Substances 0.000 title claims abstract description 49
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 31
- 230000023556 desulfurization Effects 0.000 title claims abstract description 31
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title abstract description 45
- 238000000746 purification Methods 0.000 claims abstract description 62
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000002250 absorbent Substances 0.000 claims abstract description 27
- 230000002745 absorbent Effects 0.000 claims abstract description 27
- 238000004537 pulping Methods 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims description 15
- 239000007921 spray Substances 0.000 claims description 15
- 238000004062 sedimentation Methods 0.000 claims description 7
- 238000005507 spraying Methods 0.000 claims description 7
- 239000003513 alkali Substances 0.000 claims description 4
- 238000011001 backwashing Methods 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000004064 recycling Methods 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 8
- 238000005406 washing Methods 0.000 abstract description 5
- 239000000428 dust Substances 0.000 description 8
- 230000007613 environmental effect Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- -1 condenses Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
一种水平烟道-烟囱内烟气脱硫脱硝净化装置,包括水平烟道内净化体系、烟囱内净化体系、吸收剂体系。水平烟道内净化体系是由筛板框架和筛板构成的双层无溢流筛板结构,并设有前、后挡板,使烟气从下层筛板穿过进入上层筛板,形成从下至上的双层洗涤吸收过程。烟囱内净化体系包括烟囱内底部沿斜面布置的挡水板框架、波纹挡水板和集水槽,对双侧进气体系,两侧的挡水板恰好形成V型结构。所述吸收剂系统包括沉降池、制浆池、循环泵、管路。本发明使燃煤锅炉烟气净化过程在水平烟道与烟囱内完成,简化了燃煤热电厂烟气净化系统,脱硫脱硝装置安装在烟道与烟囱内,系统占地面积减小,净化效率高,特别适宜使用在中小型燃煤热电系统的烟气净化领域。
A horizontal flue-chimney flue gas desulfurization and denitrification purification device, including a horizontal flue internal purification system, a chimney internal purification system, and an absorbent system. The internal purification system of the horizontal flue is a double-layer non-overflow sieve plate structure composed of a sieve plate frame and a sieve plate, and is equipped with a front and a rear baffle, so that the flue gas passes through the lower sieve plate and enters the upper sieve plate, forming a flow from the bottom to the upper sieve plate. The supreme double-layer washing and absorbing process. The purification system in the chimney includes the water baffle frame, the corrugated water baffle and the sump arranged along the slope at the bottom of the chimney. For the double-sided air intake system, the water baffles on both sides just form a V-shaped structure. The absorbent system includes a settling tank, a pulping tank, a circulation pump and pipelines. The invention completes the flue gas purification process of the coal-fired boiler in the horizontal flue and the chimney, simplifies the flue gas purification system of the coal-fired thermal power plant, and installs the desulfurization and denitrification device in the flue and the chimney, reduces the system footprint and improves the purification efficiency , especially suitable for use in the field of flue gas purification of small and medium-sized coal-fired thermal power systems.
Description
【技术领域】:【Technical field】:
本发明属于环境保护技术领域,特别涉及一种烟气脱硫脱硝净化装置。The invention belongs to the technical field of environmental protection, in particular to a flue gas desulfurization and denitrification purification device.
【背景技术】:【Background technique】:
我国大部分工业锅炉烟气净化多采用多管除尘器与脱硫装置串联形式,大型电厂使用多级静电除尘器与脱硫装置串联形式。对于工业锅炉,市场上也出现了一些除尘脱硫设备,但其系统不够完善并且结构存在缺陷。近几年随着排放要求的提高,一些厂家在多管除尘器后加一级简易脱硫器,脱硫除尘的效率仍不能满足现行的环保排放标准。Most of the flue gas purification of industrial boilers in my country adopts the form of multi-tube dust collector and desulfurization device in series, and large power plants use the form of multi-stage electrostatic precipitator and desulfurization device in series. For industrial boilers, some dust removal and desulfurization equipment have also appeared on the market, but their systems are not perfect and their structures are flawed. In recent years, with the improvement of emission requirements, some manufacturers have added a simple desulfurizer after the multi-tube dust collector. The efficiency of desulfurization and dust removal still cannot meet the current environmental protection emission standards.
为满足环保工程的要求,对中小型热电厂锅炉,国内脱硫产品普遍存在以下问题:设备系统繁杂,操作程序不适用于中小型用户;初投资高、运行费用大,处理后的烟气带水,引风机不能正常工作;在加碱运行时出现结垢、灰堵;烟气阻力大,能耗高,需要更换风机,烟气净化系统不能正常运行和进行有效的烟气脱硫脱硝除尘。In order to meet the requirements of environmental protection projects, for small and medium-sized thermal power plant boilers, domestic desulfurization products generally have the following problems: the equipment system is complicated, and the operating procedures are not suitable for small and medium-sized users; The induced draft fan cannot work normally; fouling and ash blockage occur during the operation of adding alkali; the flue gas resistance is large, the energy consumption is high, and the fan needs to be replaced, and the flue gas purification system cannot operate normally and perform effective flue gas desulfurization, denitrification and dust removal.
引进的烟气净化系统主要是满足大容量,高参数火电机组烟气脱硫的需要,其系统完善,运行可靠。但将此系统用于我国广大的工业锅炉与中小型燃煤热电厂的烟气净化工程存在设备费用高,运行操作复杂,运行成本高等问题。The imported flue gas purification system is mainly to meet the needs of flue gas desulfurization of thermal power units with large capacity and high parameters. Its system is complete and reliable in operation. However, there are problems such as high equipment cost, complicated operation and high operation cost when this system is used in the flue gas purification projects of my country's vast industrial boilers and small and medium-sized coal-fired thermal power plants.
在国外成熟的脱硫工艺基础上和保证正常脱硫的基础上,研制适合我国广大工业锅炉与中小型热电厂锅炉的高效、低阻及除尘、脱硫脱硝一体化的组合式净化装置是十分必要的。On the basis of foreign mature desulfurization process and normal desulfurization, it is necessary to develop a combined purification device with high efficiency, low resistance, dust removal, desulfurization and denitrification, which is suitable for the vast number of industrial boilers and small and medium-sized thermal power plant boilers in my country.
【发明内容】:本发明目的是克服现有技术存在的上述不足,提供一种水平烟道-烟囱内烟气脱硫脱硝净化装置。该装置可应用于中小型燃煤热电厂的烟气净化工程中,实现在烟道与烟囱内安装脱硫脱硝装置,可节省安装空间,节省建设资金,是一种科学的烟气净化方法。[Content of the invention]: The object of the present invention is to overcome the above-mentioned deficiencies in the prior art, and provide a horizontal flue-flue gas desulfurization and denitrification purification device in the chimney. The device can be applied to the flue gas purification project of small and medium-sized coal-fired thermal power plants. It realizes the installation of desulfurization and denitrification devices in the flue and chimney, which can save installation space and construction funds. It is a scientific flue gas purification method.
本发明提供的水平烟道-烟囱内烟气脱硫脱硝净化装置,包括设置于水平烟道内的水平烟道内净化体系和设置于烟囱内底部的烟囱内净化体系,所述水平烟道内净化体系为双层无溢流筛板结构,组成包括:筛板框架,筛板框架通过底部支撑设置于水平烟道内且不与烟道壁接触,筛板框架内设置有筛板,筛板框架前端端面及向上延伸至烟道壁设置有前挡板,筛板框架后端端面及向下延伸至烟道壁设置有后挡板,筛板框架上方设置有喷淋部件,筛板框架下方设置有反洗喷淋部件,筛板框架的前面还设置有预喷淋部件;烟囱内净化体系包括:位于水平烟道接口处的烟囱内底部沿斜面布置的挡水板框架,挡水板框架内设置有波纹挡水板,且挡水板框架与波纹挡水板迎向进气方向倾斜,挡水板框架下面设置有集水槽。在波纹挡水板的斜上方还设置有反冲洗喷淋部件。The horizontal flue-flue gas desulfurization and denitrification purification device in the chimney provided by the present invention includes a horizontal flue internal purification system arranged in the horizontal flue and a chimney internal purification system arranged at the bottom of the chimney, and the horizontal flue internal purification system is double Layer non-overflow sieve plate structure, consisting of: sieve plate frame, the sieve plate frame is set in the horizontal flue through the bottom support and does not contact the flue wall, the sieve plate frame is equipped with a sieve plate, the front end of the sieve plate frame and the upward There is a front baffle extending to the flue wall, a rear baffle is installed on the rear end of the sieve frame and extending downward to the flue wall, a spraying part is installed above the sieve frame, and a backwash spray is installed below the sieve frame. The front of the sieve plate frame is also equipped with a pre-spraying part; the purification system in the chimney includes: a water baffle frame arranged along an inclined plane at the bottom of the chimney at the interface of the horizontal flue, and a corrugated baffle is arranged in the water baffle frame The water plate, and the water retaining plate frame and the corrugated water retaining plate are inclined towards the air intake direction, and a water collection tank is arranged under the water retaining plate frame. A backwashing spray part is also arranged on the oblique upper side of the corrugated water baffle.
该净化装置同时还包括吸收剂体系,所述吸收剂体系所含部件是形成脱硫脱硝剂制备、循环、沉降与处理功能之用,其组成包括:用管路联通在一起的沉降池、制浆池和吸收剂池,水平烟道内净化体系和烟囱内净化体系中的循环液经管路流入吸收剂池后,再与制浆池中的碱液一起进入沉降池中,沉降池中的再生吸收剂被循环水泵送回净化体系循环使用。The purification device also includes an absorbent system. The components of the absorbent system are used for the preparation, circulation, sedimentation and treatment of desulfurization and denitrification agents. Pool and absorbent pool, the circulating liquid in the purification system in the horizontal flue and the purification system in the chimney flows into the absorbent pool through the pipeline, and then enters the sedimentation tank together with the lye in the pulping tank, and the regenerated absorbent in the sedimentation tank It is sent back to the purification system by the circulating water pump for recycling.
吸收剂被循环泵吸入,通过管路输送进入烟气净化体系,吸收剂与烟气中的有害气体反应,生成物随灰液进入沉降池,经过空气接触(曝气)生成沉降物与灰尘在沉降池中沉淀。循环液在流动过程中加入制浆池中的碱液与吸收剂池中的吸收剂,再生的吸收剂被循环水泵送回净化体系循环使用。在运行过程中为保证一定的净化效率,可根据回液中的pH值的变化改变吸收剂加入量。The absorbent is inhaled by the circulating pump and transported into the flue gas purification system through the pipeline. The absorbent reacts with the harmful gas in the flue gas, and the product enters the sedimentation tank along with the ash liquid, and the sediment and dust are formed after air contact (aeration). Sedimentation in the sedimentation tank. During the flowing process, the circulating liquid is added to the alkali liquor in the pulping tank and the absorbent in the absorbent tank, and the regenerated absorbent is pumped back to the purification system for recycling by the circulating water. In order to ensure a certain purification efficiency during operation, the amount of absorbent added can be changed according to the change of pH value in the return liquid.
本发明的优点和积极效果:Advantage and positive effect of the present invention:
本发明是一种节约占地空间、减少系统投资的烟气净化产品。水平烟道-烟囱内烟气脱硫脱硝净化装置利用原有热电厂建筑的混凝土烟道及烟囱,在其内部加装脱硫脱硝部件,充分利用烟道与烟囱的空间,减少脱硫脱硝塔的占地空间,简化了烟气净化系统,减少了环保投资。The invention is a flue gas purification product which saves floor space and reduces system investment. The horizontal flue-flue gas desulfurization and denitrification purification device in the chimney utilizes the concrete flue and chimney of the original thermal power plant building, and installs desulfurization and denitrification components inside to make full use of the space between the flue and chimney and reduce the floor space of the desulfurization and denitrification tower , Simplifies the flue gas purification system and reduces environmental protection investment.
本发明简化了复杂的脱硫系统,增加了脱硝功能,降低了脱硫费用,便于操作、运行可靠,可用于新建和在建锅炉的烟气净化,也可用于现有中小型热电厂锅炉的烟气净化工程改造。The invention simplifies the complex desulfurization system, increases the denitrification function, reduces the desulfurization cost, is easy to operate and reliable in operation, and can be used for flue gas purification of newly-built and under-construction boilers, and can also be used for flue gas purification of existing small and medium-sized thermal power plant boilers Engineered.
【附图说明】:[Description of drawings]:
图1为水平烟道-烟囱内烟气脱硫脱硝净化装置的横截面视图;Fig. 1 is a cross-sectional view of the flue gas desulfurization and denitrification purification device in the horizontal flue-chimney;
图2为水平烟道-烟囱内烟气脱硫脱硝净化装置的流程图。Fig. 2 is a flow chart of the flue gas desulfurization and denitrification purification device in the horizontal flue-chimney.
图中,1预喷淋部件、2前挡板、3反洗喷淋部件、4筛板框架、5后挡板、6筛板、7喷淋部件、8防腐层、9挡水板框架、10波纹挡水板、11反冲洗喷淋部件、12集水槽、13沉降池、14制浆池、15循环泵、16管路、17吸收剂池。In the figure, 1 pre-spraying part, 2 front baffle, 3 backwash spraying part, 4 sieve plate frame, 5 rear baffle, 6 sieve plate, 7 spraying part, 8 anti-corrosion layer, 9 water retaining plate frame, 10 corrugated water baffle, 11 backwashing spray parts, 12 sump, 13 settling tank, 14 pulping tank, 15 circulation pump, 16 pipeline, 17 absorbent tank.
【具体实施方式】:【Detailed ways】:
实施例1:Example 1:
本发明提供了水平烟道-烟囱内烟气脱硫脱硝净化装置,包括水平烟道内净化体系、烟囱内净化体系、吸收剂体系。The invention provides a horizontal flue-chimney flue gas desulfurization and denitrification purification device, including a horizontal flue internal purification system, a chimney internal purification system, and an absorbent system.
其中所述的水平烟道内净化体系为双层无溢流筛板结构,用于净化烟气,其组成如图1所示包括:1预喷淋部件、2前挡板、3反洗喷淋部件、4筛板框架、5后挡板、6筛板、7喷淋部件、8防腐层。The purification system in the horizontal flue described therein is a double-layer non-overflow sieve plate structure, which is used to purify the flue gas. Its composition is shown in Figure 1, including: 1 pre-spray components, 2 front baffles, 3 backwash spray Components, 4 sieve plate frame, 5 rear baffle, 6 sieve plate, 7 spray parts, 8 anti-corrosion layer.
筛板框架4,筛板框架通过底部支撑设置于水平烟道内且不与烟道壁接触,筛板框架内设置有筛板6,筛板框架前端端面及向上延伸至烟道壁设置有前挡板2,筛板框架后端端面及向下延伸至烟道壁设置有后挡板5,筛板框架上方设置有喷淋部件7,筛板框架下方设置有反洗喷淋部件3,筛板框架的前面还设置有预喷淋部件1。The
其中:预喷淋部件1为第一级烟气洗涤过程,前挡板2与后挡板5遮挡水平烟道内烟气,引导烟气进入洗涤床。筛板框架4与筛板6组成洗涤床。烟道内壁上的防腐层8为防护水平混凝土烟道的腐蚀。Among them: the pre-spray part 1 is the first-stage flue gas washing process, the
所述的烟囱内净化体系如图2所示,包括:位于水平烟道接口处的烟囱内底部沿斜面布置的挡水板框架9,挡水板框架内设置有波纹挡水板10,且挡水板框架与波纹挡水板迎向进气方向倾斜,挡水板框架下面设置有集水槽12。在波纹挡水板的斜上方还设置有反冲洗喷淋部件?11。对于双侧进气的烟囱内净化体系,其中两侧的挡水板框架与波纹挡水板组合在一起恰好形成V型结构(参见图2)。The purification system in the chimney is shown in Figure 2, comprising: a water
所述的吸收剂体系如图2所示,包括:13沉降池、14制浆池、15循环泵、16管路、17吸收剂池,形成烟气净化后的挡水除雾段。吸收剂体系所含部件是形成脱硫脱硝剂制备,脱硫脱硝剂循环、反应后的洗涤液沉降与处理功能之用,净化体系中的循环液经管路流入吸收剂池后,再与制浆池中的碱液一起进入沉降池中,沉降池中的再生吸收剂被循环水泵送回净化体系循环使用。(工作过程见发明内容部分)The absorbent system is shown in Figure 2, including: 13 settling tanks, 14 pulping tanks, 15 circulation pumps, 16 pipelines, 17 absorbent tanks, forming a water retaining and demisting section after flue gas purification. The components contained in the absorbent system are used for the preparation of desulfurization and denitrification agent, the circulation of desulfurization and denitrification agent, the settlement of washing liquid after reaction and the treatment function. The lye enters the settling tank together, and the regenerated absorbent in the settling tank is sent back to the purification system by the circulating water pump for recycling. (see the content of the invention for the working process)
工作原理working principle
高温烟气进入水平烟道后,首先被部件1预喷淋加湿雾化,烟气被加湿冷却,烟尘与水雾碰撞,凝结,粒化,烟气中的二氧化硫及氮氧化物被碱液吸收,形成第一级净化。After the high-temperature flue gas enters the horizontal flue, it is first pre-sprayed, humidified and atomized by part 1, the flue gas is humidified and cooled, the flue dust collides with the water mist, condenses, granulates, and the sulfur dioxide and nitrogen oxides in the flue gas are absorbed by the lye , forming the first stage of purification.
水平烟道内净化体系采用二级无溢流分组筛板结构,形成有效沸腾床通流形态,增加烟气与吸收剂的反应时间,使烟气与吸收液充分混合接触。通流结构的流通截面经过多项工程使用,脱硫效果满足排放标准。The purification system in the horizontal flue adopts a two-stage non-overflow grouped sieve plate structure to form an effective fluidized bed flow form, increase the reaction time between the flue gas and the absorbent, and fully mix and contact the flue gas and the absorption liquid. The flow section of the flow structure has been used in many projects, and the desulfurization effect meets the emission standards.
携带烟尘和水雾的烟气通过部件3反洗喷淋与部件6筛板后,烟气与碱液高速碰撞,气流将以珠状通过沸腾液面,烟气与吸收液的有效接触面积增加,在烟气与碱液接触过程中形成了更有效的吸收过程。烟气经过吸收后向上流动,与上层筛板滴下的吸收剂形成碰撞,进而加强混合,在此流动过程中形成反应过程。当烟气进入二级筛板后形成与前级相似的反应过程。After the flue gas carrying smoke dust and water mist passes through the backwash spray of
在装置上部设部件7喷淋设备,烟气在净化的同时与下降的吸收剂进一步接触进行反应,提高装置运行的可靠性。Component 7 spray equipment is installed on the upper part of the device, and the flue gas is further contacted and reacted with the falling absorbent while being purified, so as to improve the reliability of the device operation.
净化后的烟气进入烟囱内净化体系,该体系对净化后的烟气进行除雾,除去烟气中的液珠,保证排烟中不含液态水分。除雾器采用高级工程塑料,并设置冲洗装置,保证除雾器不堵塞不结垢。The purified flue gas enters the purification system in the chimney, which demistes the purified flue gas, removes liquid droplets in the flue gas, and ensures that the exhaust gas does not contain liquid moisture. The demister is made of high-grade engineering plastics, and a flushing device is installed to ensure that the demister is not blocked or scaled.
固化物在沉降池中沉淀,澄清液处理后被循环水泵送回使用。在运行过程中为保证可靠的净化效率,可根据回液中的pH值的变化改变加碱量(保证回液的pH值一定)。调整pH值后碱液送回设备,脱硫剂与循环水循环使用。The solidified matter settles in the settling tank, and the clarified liquid is sent back to use by the circulating water pump after being treated. In order to ensure reliable purification efficiency during operation, the amount of alkali added can be changed according to the change of the pH value in the return liquid (to ensure that the pH value of the return liquid is constant). After adjusting the pH value, the lye is sent back to the equipment, and the desulfurizer and circulating water are recycled.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201010031308A CN101721901A (en) | 2010-01-05 | 2010-01-05 | Flue gas desulfurization and denitration purifying device in chimney of horizontal flue |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201010031308A CN101721901A (en) | 2010-01-05 | 2010-01-05 | Flue gas desulfurization and denitration purifying device in chimney of horizontal flue |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101721901A true CN101721901A (en) | 2010-06-09 |
Family
ID=42443813
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201010031308A Pending CN101721901A (en) | 2010-01-05 | 2010-01-05 | Flue gas desulfurization and denitration purifying device in chimney of horizontal flue |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101721901A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102688644A (en) * | 2012-02-23 | 2012-09-26 | 庄建中 | Dedusting, desulfurization and denitrification environment-friendly chimney |
CN103644604A (en) * | 2013-12-03 | 2014-03-19 | 王骞 | Air PM dedusting sterilizer |
CN112058055A (en) * | 2020-08-18 | 2020-12-11 | 上海交通大学 | Buffer type intermittent acidolysis flue gas purification device and process |
CN112413731A (en) * | 2019-08-22 | 2021-02-26 | 广东美的制冷设备有限公司 | Air purification module and air conditioner indoor unit |
CN112516773A (en) * | 2019-09-18 | 2021-03-19 | 北京绿岸壹号能源科技有限公司 | Spray purification device |
-
2010
- 2010-01-05 CN CN201010031308A patent/CN101721901A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102688644A (en) * | 2012-02-23 | 2012-09-26 | 庄建中 | Dedusting, desulfurization and denitrification environment-friendly chimney |
CN103644604A (en) * | 2013-12-03 | 2014-03-19 | 王骞 | Air PM dedusting sterilizer |
CN112413731A (en) * | 2019-08-22 | 2021-02-26 | 广东美的制冷设备有限公司 | Air purification module and air conditioner indoor unit |
CN112516773A (en) * | 2019-09-18 | 2021-03-19 | 北京绿岸壹号能源科技有限公司 | Spray purification device |
CN112058055A (en) * | 2020-08-18 | 2020-12-11 | 上海交通大学 | Buffer type intermittent acidolysis flue gas purification device and process |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103185346B (en) | Waste incineration flue gas combined purification system and its technology | |
CN202823151U (en) | Multistage spray efficient wet process of flue gas desulfurization and synergistic mercury removal integrated device | |
CN204865480U (en) | High -efficient desulfurization, denitration, dust removal and water conservation integration process systems | |
CN103830986A (en) | Integrated dust removal-purification device and purification method of stationary diesel engine system | |
CN102974185A (en) | Modularized integrated smoke purification system and method for removing plurality of pollutants | |
CN204320062U (en) | A kind of high effective flue gas cleaning system | |
CN105214465A (en) | The apparatus and method of integration wet process of FGD dedusting | |
CN1597059A (en) | Twin-tower circulation washing and suction smoke and desulfurization method for waste water of power plant boiler | |
CN206276171U (en) | A kind of high-efficiency flue gas desulfurization cleaner | |
CN101721901A (en) | Flue gas desulfurization and denitration purifying device in chimney of horizontal flue | |
CN1899675A (en) | Reverse flow type seawater desulfurizing and absorption tower | |
CN104258668A (en) | Deep washing dust removal device | |
CN204182256U (en) | A kind of washing degree of depth dust arrester | |
CN205796820U (en) | A kind of desulfurating dust-removing equipment | |
CN201105203Y (en) | Ring grid showering spume dust removing and desulferizing device | |
CN209828704U (en) | Boiler flue gas can condense particulate matter and get rid of heat recovery system in coordination | |
CN2875572Y (en) | Dust collecting sulfur gathering circulation device in smoke dust discharge | |
CN105299674B (en) | A kind of Multifunctional smoke energy-saving and emission-reduction system | |
CN207694528U (en) | Industrial tail gas flue dust and formaldehyde comprehensive treatment system | |
CN101927125A (en) | Dual-circulation absorption tower | |
CN205360936U (en) | A condensing takes off dirt defogging device for wet flue gas desulfurization system | |
CN205055798U (en) | Modular wet -type flue gas desulfurization dust collector | |
CN205055799U (en) | Device that integration wet flue gas desulfurization removed dust | |
CN207356902U (en) | One kind catalysis denitrating flue gas desulfurizer | |
CN205065765U (en) | Multi -functional flue gas energy saving and emission reduction system |
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 |
Open date: 20100609 |