CN201094885Y - High concentration bag-type dust remover - Google Patents
High concentration bag-type dust remover Download PDFInfo
- Publication number
- CN201094885Y CN201094885Y CNU2007200867341U CN200720086734U CN201094885Y CN 201094885 Y CN201094885 Y CN 201094885Y CN U2007200867341 U CNU2007200867341 U CN U2007200867341U CN 200720086734 U CN200720086734 U CN 200720086734U CN 201094885 Y CN201094885 Y CN 201094885Y
- Authority
- CN
- China
- Prior art keywords
- dust
- bag
- smoke
- flue gas
- gas
- 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.)
- Expired - Lifetime
Links
- 239000000428 dust Substances 0.000 title abstract description 31
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 19
- 239000003546 flue gas Substances 0.000 claims description 19
- 238000005192 partition Methods 0.000 claims description 6
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 3
- 239000000779 smoke Substances 0.000 abstract description 3
- 239000002131 composite material Substances 0.000 abstract description 2
- 238000007664 blowing Methods 0.000 abstract 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
-
- 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
Description
技术领域technical field
本实用新型涉及一种袋式除尘器,特别涉及一种用于去除烟气中粉尘浓度高的袋式除尘器。The utility model relates to a bag type dust remover, in particular to a bag type dust remover used for removing high dust concentration in flue gas.
背景技术Background technique
随着人们对粉尘污染认识的提高,排放标准将越来越严格,一些地方要求经处理后的烟气中粉尘含量必须低于50mg/m3,这就对除尘装置提出了更高的要求。With the improvement of people's awareness of dust pollution, the emission standards will become more and more stringent. Some places require that the dust content in the treated flue gas must be lower than 50mg/m 3 , which puts forward higher requirements for dust removal devices.
目前对于高浓度粉尘的治理仍缺乏合适的处理技术和装置,传统的粉尘去除装置通常存在系统复杂,占地面积大,运行费用高等普遍问题,特别是对微细粉尘捕集效率低。At present, there is still a lack of suitable treatment technology and devices for the treatment of high-concentration dust. Traditional dust removal devices usually have common problems such as complex systems, large footprints, and high operating costs, especially for the low collection efficiency of fine dust.
袋式除尘器是高效控制微细粒子排放的设备。常规袋式除尘器处理烟气浓度一般在100g/nm3以下。但用于干法脱硫的袋式除尘器入口烟气粉尘浓度高达500~2000g/nm3,因此,常规袋式除尘器不能用于高浓度的场合。The bag filter is an efficient device for controlling the emission of fine particles. The concentration of flue gas treated by conventional bag filter is generally below 100g/nm 3 . However, the inlet flue gas dust concentration of the bag filter used for dry desulfurization is as high as 500-2000g/nm 3 , so the conventional bag filter cannot be used in high concentration occasions.
发明内容Contents of the invention
本实用新型的目的是提供一种高浓度袋式除尘器,使袋式除尘器适应烟气中粉尘浓度高的场合,同时提高袋式除尘器对微细粉尘的捕集效率,满足粉尘排放标准的要求。The purpose of this utility model is to provide a high-concentration bag-type dust collector, so that the bag-type dust collector can adapt to the occasion with high dust concentration in the flue gas, and at the same time improve the collection efficiency of the bag-type dust collector for fine dust and meet the requirements of the dust discharge standard. Require.
本实用新型的技术解决方案是:The technical solution of the utility model is:
一种高浓度袋式除尘器,包括烟气进口、壳体、滤袋、上箱体、脉冲喷吹装置、灰斗、卸灰阀、烟气出口,在壳体内靠近烟气进口处垂直设置隔板,将袋式除尘器壳体分割出一部分,这部分相当于形成了一个机械沉降室,对高浓度的粉尘进行一个预处理,使较大颗粒的粉尘沉降下来,然后再在隔板的后面平行设置气流分布器,气流分布器起到整流的作用,便于滤袋提高过滤效率,从而提高对微细粉尘的捕集效率。A high-concentration bag filter, including a flue gas inlet, a shell, a filter bag, an upper box, a pulse injection device, an ash hopper, an ash discharge valve, and a flue gas outlet, which are vertically arranged in the shell close to the flue gas inlet The clapboard divides the shell of the bag filter into a part, which is equivalent to forming a mechanical settling chamber, which pre-treats the high-concentration dust and settles the larger particles of dust, and then puts them on the clapboard. The air distributor is arranged in parallel at the back, and the air distributor plays the role of rectification, which is convenient for the filter bag to improve the filtration efficiency, thereby improving the collection efficiency of fine dust.
本实用新型的有益效果是:采用机械除尘与袋式除尘复合技术,提高了除尘效率,同时运行稳定,除尘效率可达99%以上。The beneficial effect of the utility model is that: the composite technology of mechanical dust removal and bag type dust removal is adopted to improve the dust removal efficiency, and at the same time, the operation is stable, and the dust removal efficiency can reach more than 99%.
附图说明Description of drawings
图1高浓度袋式除尘器结构图Figure 1 Structural diagram of high concentration bag filter
图中1.烟气进口,2.隔板,3.气流分布器,4.滤袋,5.脉冲喷吹装置,6.上箱体,7.烟气出口,8.壳体,9.灰斗,10.卸灰阀In the figure 1. Smoke inlet, 2. Partition, 3. Air distributor, 4. Filter bag, 5. Pulse injection device, 6. Upper box, 7. Smoke outlet, 8. Shell, 9. Ash hopper, 10. Ash discharge valve
具体实施方式Detailed ways
下面对本实用新型做进一步的说明:The utility model is described further below:
一种高浓度袋式除尘器,由烟气进口1、壳体8、滤袋4、上箱体6、脉冲喷吹装置5、灰斗9、卸灰阀10、烟气出口7构成,在壳体8内靠近进口1处垂直设置隔板2,在隔板2后面平行设置气流分布器3。A high-concentration bag-type dust collector consists of a flue gas inlet 1, a housing 8, a filter bag 4, an upper box 6, a pulse injection device 5, an ash hopper 9, an ash discharge valve 10, and a flue gas outlet 7. A partition 2 is arranged vertically near the inlet 1 in the housing 8 , and an airflow distributor 3 is arranged in parallel behind the partition 2 .
使用时,高浓度含尘烟气自上而下经烟气进口1进入袋式除尘器,在隔板2所形成的预分离空间进行预分离,分离下来的粉尘落入灰斗9;烟气再经气流分布器3实现整流。整流后的烟气通过滤袋4进行过滤。过滤后的烟气汇集到上箱体6,从烟气出口7排出。When in use, the high-concentration dust-containing flue gas enters the bag filter from top to bottom through the flue gas inlet 1, and performs pre-separation in the pre-separation space formed by the partition 2, and the separated dust falls into the ash hopper 9; the flue gas Rectification is realized through the air distributor 3 . The rectified flue gas is filtered through the filter bag 4 . The filtered flue gas is collected into the upper box body 6 and discharged from the flue gas outlet 7.
随着过滤的进行,滤袋阻力增加,需进行清灰。清灰通过脉冲喷吹装置5实现。滤袋表面灰尘脱落掉到灰斗9,通过卸灰阀10排除。As the filtration progresses, the resistance of the filter bag increases and dust removal is required. Dust removal is realized by pulse injection device 5. The dust on the surface of the filter bag falls off to the ash hopper 9 and is discharged through the ash discharge valve 10.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200867341U CN201094885Y (en) | 2007-08-29 | 2007-08-29 | High concentration bag-type dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200867341U CN201094885Y (en) | 2007-08-29 | 2007-08-29 | High concentration bag-type dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201094885Y true CN201094885Y (en) | 2008-08-06 |
Family
ID=39921943
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200867341U Expired - Lifetime CN201094885Y (en) | 2007-08-29 | 2007-08-29 | High concentration bag-type dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201094885Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103316555A (en) * | 2013-05-21 | 2013-09-25 | 溧阳市正翔精密机械有限公司 | Circulation reflux dedusting structure, and mobile circulation reflux industrial vacuum cleaner |
| CN103752121A (en) * | 2014-01-28 | 2014-04-30 | 浙江吉天环保科技有限公司 | Combined dust remover applied to high-concentration dust |
| CN103768884A (en) * | 2014-02-11 | 2014-05-07 | 湖南省粮油科学研究设计院 | Two-stage combined dust remover capable of treating flexible impurities |
| CN105032057A (en) * | 2015-09-01 | 2015-11-11 | 启东市洁华环保机械厂 | Shower head cloth bag dust removing device |
| CN106823598A (en) * | 2016-12-23 | 2017-06-13 | 易能环境技术有限公司 | One kind is straight-through to flow pulse bag type dust collector |
| CN108434883A (en) * | 2018-06-12 | 2018-08-24 | 盐城诚达环保工程有限公司 | The pocket type pulsed dust collector that can cool down |
-
2007
- 2007-08-29 CN CNU2007200867341U patent/CN201094885Y/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103316555A (en) * | 2013-05-21 | 2013-09-25 | 溧阳市正翔精密机械有限公司 | Circulation reflux dedusting structure, and mobile circulation reflux industrial vacuum cleaner |
| CN103316555B (en) * | 2013-05-21 | 2015-04-29 | 溧阳市正翔精密机械有限公司 | Circulation reflux dedusting structure, and mobile circulation reflux industrial vacuum cleaner |
| CN103752121A (en) * | 2014-01-28 | 2014-04-30 | 浙江吉天环保科技有限公司 | Combined dust remover applied to high-concentration dust |
| CN103768884A (en) * | 2014-02-11 | 2014-05-07 | 湖南省粮油科学研究设计院 | Two-stage combined dust remover capable of treating flexible impurities |
| CN105032057A (en) * | 2015-09-01 | 2015-11-11 | 启东市洁华环保机械厂 | Shower head cloth bag dust removing device |
| CN106823598A (en) * | 2016-12-23 | 2017-06-13 | 易能环境技术有限公司 | One kind is straight-through to flow pulse bag type dust collector |
| CN108434883A (en) * | 2018-06-12 | 2018-08-24 | 盐城诚达环保工程有限公司 | The pocket type pulsed dust collector that can cool down |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20080806 |