CN2912767Y - Cloth bag dust remover - Google Patents
Cloth bag dust remover Download PDFInfo
- Publication number
- CN2912767Y CN2912767Y CN200620118052.XU CN200620118052U CN2912767Y CN 2912767 Y CN2912767 Y CN 2912767Y CN 200620118052 U CN200620118052 U CN 200620118052U CN 2912767 Y CN2912767 Y CN 2912767Y
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- air
- filter
- bag
- plate
- partition
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- 239000000428 dust Substances 0.000 title abstract description 27
- 239000004744 fabric Substances 0.000 title 1
- 238000005192 partition Methods 0.000 claims abstract description 15
- 238000013016 damping Methods 0.000 claims abstract description 11
- 238000009423 ventilation Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 description 7
- 239000004568 cement Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
一种布袋除尘器,它包括两端分别设有进风口和出风口的箱体,在箱体内装有花板和滤袋构成的过滤装置,并与箱体顶面构成净气室,过滤装置的进气方、下方和中间形成气流通道;其中进风口内设有阻尼均风板,在箱体进风端紧邻滤袋之处,沿竖直方向设有隔板,在阻尼均风板和隔板之间设有反射板,在阻尼均风板上,在隔板的二侧边和中间部位的竖直方向上都均匀分布地分别开有若干个通气孔。本实用新型布袋除尘器,经测试,除尘器的运行阻力从1500~1800Pa降低到1500~1800Pa,降低了300Pa,还节约动力消耗10~15%,也延长了滤袋的使用寿命。
A bag filter, which includes a box body with air inlets and outlets at both ends, a filter device composed of a flower plate and a filter bag is installed in the box body, and a clean air chamber is formed with the top surface of the box body, and the filter device Airflow channels are formed at the air intake side, below and in the middle; among them, a damping air distribution plate is arranged in the air inlet, and a partition is arranged in the vertical direction at the air inlet end of the box close to the filter bag, and the damping air distribution board and the Reflecting plates are arranged between the partitions, and a plurality of ventilation holes are evenly distributed on the vertical direction of the two sides and the middle part of the partitions on the damping air equalizing plate. The bag dust collector of the utility model has been tested, and the running resistance of the dust collector has been reduced from 1500-1800Pa to 1500-1800Pa, which is 300Pa lower, and also saves power consumption by 10-15%, and also prolongs the service life of the filter bag.
Description
技术领域technical field
本实用新型涉及一种除尘器,具体说是广泛用于火力发电厂、水泥厂等含尘废气环境的处理设备。The utility model relates to a dust remover, in particular to processing equipment widely used in dust-containing waste gas environments such as thermal power plants and cement plants.
背景技术Background technique
火力发电厂、水泥厂等燃烧设备中,静电式除尘器和布袋式脉冲除尘器在含尘废气的处理中得到广泛地应用,其中布袋式脉冲除尘器包括箱体和在箱体中安装的滤袋,安装在箱体上的喷吹系统和脉冲控制系统,以及出风口中的调风阀等。进入箱体中的含尘废气中稍大颗粒的高温粉沫直接落入灰斗,在调风阀的调节下,含微尘废气由箱体下部进入布满滤袋的过滤室,通过大面积的滤袋的过滤作用,将微尘滞留在滤袋的外表面上,经滤袋过滤后的废气从箱体上部经出风口排出。由于气流在箱体内部的运行速度快、阻力大(一般均达到1500~1800Pa),所以除尘设备运行的动力消耗较高。又由于调风阀出口风速较高,下进风时极易引起二次扬尘,增加了废气中的含尘浓度,显然又加大了运行负荷。In combustion equipment such as thermal power plants and cement plants, electrostatic precipitators and bag-type pulse dust collectors are widely used in the treatment of dusty waste gas. Among them, the bag-type pulse dust collector includes a box and a filter installed in the box. bag, the injection system and pulse control system installed on the box, and the air regulating valve in the air outlet, etc. The slightly larger particles of high-temperature powder in the dust-laden exhaust gas entering the box directly fall into the ash hopper. Under the adjustment of the air regulating valve, the dust-laden exhaust gas enters the filter chamber covered with filter bags from the lower part of the box body, and passes through a large area. The filtering effect of the special filter bag keeps the dust on the outer surface of the filter bag, and the exhaust gas filtered by the filter bag is discharged from the upper part of the box through the air outlet. Due to the fast running speed and high resistance of the airflow inside the box (generally reaching 1500-1800Pa), the power consumption of the dust removal equipment is relatively high. And because of the high wind speed at the outlet of the damper, it is easy to cause secondary dust when the wind enters downward, which increases the dust concentration in the exhaust gas and obviously increases the operating load.
实用新型内容Utility model content
本实用新型要解决的技术问题是提供一种能有效地降低运行阻力,防止二次扬尘产尘的布袋除尘器,从而达到节约动力消耗的目的。The technical problem to be solved by the utility model is to provide a bag filter that can effectively reduce running resistance and prevent secondary dust generation, thereby achieving the purpose of saving power consumption.
本实用新型布袋除尘器,包括两端分别设有进风口和出风口的箱体,在箱体内装有过滤装置,该装置包括花板和若干个竖直安放的滤袋,每个滤袋上端分别与花板上均匀分布排列的通孔固定连接,水平安放的花板与箱体上部封闭连接,并与箱体顶面构成净气室,过滤装置的进气方、下方和中间形成气流通道;其中进风口包括与箱体一端连为一体的锥形壳体,在锥形壳体内,沿进风口轴线相互垂直的方向上设有阻尼均风板,该板周边与锥形壳体封闭连接,板面上均匀分布地开有若干个通气孔;在箱体进风端紧邻滤袋之处,沿竖直方向设有隔板,隔板的下端悬空,其余各边均与箱体内壁连接固定,在隔板的二侧边和中间部位的竖直方向上也均匀分布地分别开有若干个通气孔。The bag filter of the utility model comprises a box body with air inlets and air outlets at both ends, and a filter device is installed in the box body. The device includes flower plates and several filter bags placed vertically. They are respectively fixedly connected to the evenly distributed through holes on the flower board, and the horizontally placed flower board is closed and connected to the upper part of the box body, and forms a clean air chamber with the top surface of the box body, and the air intake side, bottom and middle of the filter device form an air flow channel The air inlet includes a conical shell connected to one end of the box body. In the conical shell, a damping air distribution plate is arranged along the direction perpendicular to the axis of the air inlet. The periphery of the plate is closed and connected with the conical shell. , there are a number of air holes evenly distributed on the board surface; at the place where the air inlet end of the box is close to the filter bag, there is a partition along the vertical direction, the lower end of the partition is suspended, and the other sides are connected to the inner wall of the box Fixed, on the vertical direction of the two side edges and the middle part of the dividing plate, several air holes are also evenly distributed respectively.
本实用新型布袋除尘器,其中在阻尼均风板和隔板之间,与隔板相对应的范围内设有沿竖直方向排列、且两端与壳体固定连接、水平方向安放的若干块反射板,且反射板具有向下倾斜的折弯边。The bag dust collector of the utility model, wherein between the damping air uniform plate and the partition, there are several blocks arranged in the vertical direction, fixedly connected with the shell at both ends, and placed in the horizontal direction within the range corresponding to the partition. A reflective plate, and the reflective plate has a downwardly inclined bent edge.
本实用新型布袋除尘器,其中在隔板中间部位、沿过滤装置中间的气流通道,竖直方向对称地设有两块导风板。The bag dust collector of the utility model is provided with two air guide plates symmetrically in the vertical direction along the air flow channel in the middle of the partition plate.
本实用新型布袋除尘器,是在进风口处设置阻尼均风装置和导风系统,废气流通过的面积增加了近10倍,使气流速度下降到小于1米/秒,由于气流速度较低,且分布均匀,含尘废气的浓度得到显著下降,且有效地抑制了二次扬尘的产生,使通过滤袋的废气中粉尘浓度大大降低,在同样脉冲周期内降低过滤阻力,提高滤袋的使用寿命。经测试,除尘器的运行阻力从1500~1800Pa降低到1200~1500Pa,降低了300Pa,还节约动力消耗10~15%,也延长了滤袋的使用寿命。The bag dust collector of the utility model is equipped with a damping air equalizing device and an air guide system at the air inlet, and the area through which the exhaust gas flows is increased by nearly 10 times, so that the air flow speed is reduced to less than 1 m/s. Due to the low air flow speed, And the distribution is uniform, the concentration of dusty exhaust gas is significantly reduced, and the generation of secondary dust is effectively suppressed, so that the dust concentration in the exhaust gas passing through the filter bag is greatly reduced, the filter resistance is reduced in the same pulse cycle, and the use of the filter bag is improved. life. After testing, the running resistance of the dust collector has been reduced from 1500-1800Pa to 1200-1500Pa, a reduction of 300Pa, which also saves power consumption by 10-15%, and prolongs the service life of the filter bag.
附图说明Description of drawings
图1为本实用新型布袋除尘器原理构造示意图(箱体为剖面);Fig. 1 is a schematic diagram of the principle structure of the bag filter of the present invention (casing is a section);
图2为图1的A-A剖面示意图;Fig. 2 is the A-A sectional schematic diagram of Fig. 1;
图3为图1的B-B剖面示意图。FIG. 3 is a schematic cross-sectional view along line B-B of FIG. 1 .
具体实施方式Detailed ways
由图1~图3可见,本实用新型布袋除尘器包括两端分别设有进风口1和出风口2的箱体3,其中进风口1包括与箱体3一端连为一体的锥形壳体10,在锥形壳体10内,沿进风口1轴线相互垂直的方向上设有阻尼均风板11,该板四周与锥形壳体10封闭连接,板面上均匀分布地开有若干个通气孔,构成一级阻尼均风系统,含尘气流通过后,气流速度降到1m/s以下。再经沿竖直方向排列、且两端与壳体10固定连接、水平方向安放的若干块向下倾斜的折弯反射板13构成的预沉降系统,使含尘气流中稍大颗粒的高温粉尘受反射板13的阻档,直接落入下面的灰斗9中。在箱体3内装有过滤装置,该装置包括若干个竖直安放的滤袋4和花板5,以及固定支架,每个滤袋4上端分别与花板5上均匀分布排列的通孔固定连接,水平安放的花板5与箱体3上部封闭连接,并与箱体3顶面构成净气室6,即箱体3的中下部通过滤袋4与上部的净气室6连通。过滤装置的进气方、下方和中间形成气流通道,含微尘的气流在隔板12的引导下,大部分自下而上经滤袋4过滤后进入净气室6;另一部分通过隔板12两侧边和中心部位的通气孔所构成的二级阻尼均风系统,经滤袋4过滤后进入净气室6,最后经出风通道7和出风阀8,从出风口2排出。It can be seen from Figures 1 to 3 that the bag filter of the present invention includes a
当滤袋4表面粉尘达到一定厚度时,控制系统发出清灰指令,压缩空气通过安装在箱体3顶部的喷吹装置15和脉冲阀16,对滤袋4进行在线清灰。滤袋4为化纤材料制成的过滤棒。当布袋灰斗9装满粉尘时,通过安装在其上的振打器作用,将粉尘卸出。When the dust on the surface of the
本实用新型在一发电机组实施处理中,经环保部门测试,除尘器进口含尘浓度为46g/Nm3,出口的浓度下降到27mg/Nm3,达到设计要求。The utility model is implemented in a generating unit, and the environmental protection department tests that the dust concentration at the inlet of the dust collector is 46g/Nm 3 , and the concentration at the outlet drops to 27mg/Nm 3 , meeting the design requirements.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200620118052.XU CN2912767Y (en) | 2006-06-08 | 2006-06-08 | Cloth bag dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200620118052.XU CN2912767Y (en) | 2006-06-08 | 2006-06-08 | Cloth bag dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2912767Y true CN2912767Y (en) | 2007-06-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200620118052.XU Expired - Fee Related CN2912767Y (en) | 2006-06-08 | 2006-06-08 | Cloth bag dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2912767Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101507890B (en) * | 2009-02-12 | 2010-12-29 | 武汉凯迪电力环保有限公司 | Straight-through blocking bag filter |
| CN101396629B (en) * | 2007-09-27 | 2011-11-30 | 贵阳铝镁设计研究院有限公司 | Cloth bag dust remover and production method |
| CN102553360A (en) * | 2010-06-30 | 2012-07-11 | 广州迪森热能技术股份有限公司 | Biomass ash bag deduster |
| CN105233572A (en) * | 2015-10-31 | 2016-01-13 | 安阳工学院 | Automatic flue dedusting apparatus |
| CN110252073A (en) * | 2019-07-23 | 2019-09-20 | 陈美青 | Deduster |
-
2006
- 2006-06-08 CN CN200620118052.XU patent/CN2912767Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101396629B (en) * | 2007-09-27 | 2011-11-30 | 贵阳铝镁设计研究院有限公司 | Cloth bag dust remover and production method |
| CN101507890B (en) * | 2009-02-12 | 2010-12-29 | 武汉凯迪电力环保有限公司 | Straight-through blocking bag filter |
| CN102553360A (en) * | 2010-06-30 | 2012-07-11 | 广州迪森热能技术股份有限公司 | Biomass ash bag deduster |
| CN102553360B (en) * | 2010-06-30 | 2014-05-28 | 广州迪森热能技术股份有限公司 | Biomass ash bag deduster |
| CN105233572A (en) * | 2015-10-31 | 2016-01-13 | 安阳工学院 | Automatic flue dedusting apparatus |
| CN105233572B (en) * | 2015-10-31 | 2018-02-13 | 安阳工学院 | One kind automation flue cleaner |
| CN110252073A (en) * | 2019-07-23 | 2019-09-20 | 陈美青 | Deduster |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070620 |