CN201664549U - Rotary low pressure air volume pulse bag filter - Google Patents
Rotary low pressure air volume pulse bag filter Download PDFInfo
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- CN201664549U CN201664549U CN2010200227309U CN201020022730U CN201664549U CN 201664549 U CN201664549 U CN 201664549U CN 2010200227309 U CN2010200227309 U CN 2010200227309U CN 201020022730 U CN201020022730 U CN 201020022730U CN 201664549 U CN201664549 U CN 201664549U
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- 239000000428 dust Substances 0.000 claims abstract description 32
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000003546 flue gas Substances 0.000 claims abstract description 18
- 238000002347 injection Methods 0.000 claims abstract description 14
- 239000007924 injection Substances 0.000 claims abstract description 14
- 238000004140 cleaning Methods 0.000 claims abstract description 9
- 238000003860 storage Methods 0.000 claims abstract description 8
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 4
- 238000005192 partition Methods 0.000 claims description 4
- 238000007664 blowing Methods 0.000 abstract description 10
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 2
- 239000007921 spray Substances 0.000 abstract description 2
- 238000009826 distribution Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
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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
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- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
本实用新型涉及一种旋转式低压大气量脉冲袋式除尘器,包含机箱、净气室、灰斗、机箱顶部与净气室之间的花板及安装在花板上并成束排列的多条滤袋,机箱设有烟气进口和净气室净烟气出口,滤袋束的上方设有由脉冲阀、储气罐、旋转风管和水平喷吹岔管组成的清灰组件,所说的风管与旋转电机和减速器相连而可带动水平喷吹岔管一同旋转。水平喷吹岔管在旋转状态下喷吹脉冲压缩空气,每组滤袋束只需对应设置一个脉冲清灰组件,即能完成该花板上全部滤袋的清灰,安装维修方便,结构紧凑,节省材料。本袋式除尘器可在同一箱体内紧凑地设置多个由花板固定的滤袋束,可用于特大流量的烟气除尘,低能耗,高效率,降低除尘成本。
The utility model relates to a rotary low-pressure large-capacity pulse bag-type dust collector, which comprises a machine case, a clean air chamber, an ash hopper, a flower plate between the top of the machine case and the clean air chamber, and multi- The chassis is equipped with a flue gas inlet and a net flue gas outlet of the clean air chamber. Above the filter bag bundle is a dust removal assembly consisting of a pulse valve, an air storage tank, a rotating air pipe and a horizontal injection branch pipe. Said air pipe is connected with the rotating motor and the reducer so as to drive the horizontal blowing branch pipe to rotate together. The horizontal blowing branch pipe sprays pulsed compressed air in a rotating state, and each group of filter bag bundles only needs to be equipped with a corresponding pulse cleaning component to complete the cleaning of all filter bags on the flower plate. It is easy to install and maintain, and has a compact structure. , saving material. This bag type dust collector can compactly set multiple filter bag bundles fixed by flower plates in the same box, which can be used for flue gas dust removal with large flow rate, low energy consumption, high efficiency, and reduced dust removal cost.
Description
技术领域technical field
本实用新型涉及一种袋式除尘设备,尤其涉及旋转式低压大气量脉冲袋式除尘器,属于气固分离设备。The utility model relates to a bag-type dedusting device, in particular to a rotary low-pressure large-volume pulse bag-type dedusting device, which belongs to gas-solid separation equipment.
背景技术Background technique
袋式除尘器用于电力、水泥、冶金、垃圾焚烧、建材等行业的烟气净化,含尘气体通过滤袋过滤,烟气中的粉尘被阻挡在滤袋外,通过清灰系统将粉尘吹落入灰斗,洁净烟气从滤袋内穿过,通过净气室排放大气。目前,袋式除尘设备是在滤袋顶部设一根固定的反吹清灰风管,每一根反吹风管由一个小型脉冲阀控制,喷吹能力低,只能用于较短的滤袋,因此整台除尘设备需设置大量反吹风管和脉冲阀,少则数十个,多则上百个,导致钢材耗量多,造价高,检修维护工作繁琐。使烟气除尘成本大增。近年来,随着经济的快速增长,电厂等企业规模不断扩大,排烟量也骤增,常规的袋式除尘设备由于除尘效率低,能耗高,设备体积十分庞大,已不能适应大型企业的烟气除尘处理。The bag filter is used for flue gas purification in industries such as electric power, cement, metallurgy, waste incineration, and building materials. The dusty gas is filtered through the filter bag, and the dust in the flue gas is blocked outside the filter bag, and the dust is blown off by the dust cleaning system. Into the ash hopper, the clean flue gas passes through the filter bag, and is discharged into the atmosphere through the clean air chamber. At present, the bag-type dust removal equipment is equipped with a fixed back-blowing and dust-cleaning air pipe on the top of the filter bag. Each back-blowing pipe is controlled by a small pulse valve, and the blowing capacity is low, so it can only be used for shorter filter bags. , so the entire dust removal equipment needs to be equipped with a large number of anti-blow pipes and pulse valves, ranging from dozens to hundreds, resulting in high steel consumption, high cost, and cumbersome maintenance work. The cost of flue gas dust removal is greatly increased. In recent years, with the rapid economic growth, the scale of power plants and other enterprises has continued to expand, and the amount of smoke exhaust has also increased sharply. Conventional bag-type dust removal equipment has low dust removal efficiency, high energy consumption, and very large equipment volume, which can no longer adapt to the needs of large enterprises. Flue gas dust removal treatment.
发明内容Contents of the invention
本实用新型的目的是,提供一种旋转式低压大气量脉冲袋式除尘器,通过优化设计,提高除尘效率,减小设备体积,降低能耗,节约投资。降低成本。The purpose of this utility model is to provide a rotary low-pressure large-volume pulse bag dust collector, which can improve dust removal efficiency, reduce equipment volume, reduce energy consumption and save investment through optimized design. cut costs.
本实用新型袋式除尘器包含机箱、净气室、灰斗、花板及安装在花板上并成束排列的多条滤袋,机箱设有烟气进气喇叭口,净气室设有净烟气出气喇叭口,滤袋束的上方设有由脉冲阀、储气罐、风管和水平喷吹岔管组成的清灰组件,所说的风管与旋转电机和减速器相连而可带动水平喷吹岔管一同旋转。The bag-type dust collector of the utility model includes a chassis, a clean air chamber, an ash hopper, a flower plate and a plurality of filter bags arranged on the flower plate and arranged in bundles. The clean flue gas exits the bell mouth, and above the filter bag bundle is a dust cleaning assembly consisting of a pulse valve, an air storage tank, an air pipe and a horizontal injection branch pipe. The air pipe is connected with a rotating motor and a reducer. Drive the horizontal injection branch pipe to rotate together.
同一箱体顶部设有多个花板,每个花板均装有滤袋束并配置一套清灰组件。There are multiple flower plates on the top of the same box, and each flower plate is equipped with a filter bag bundle and equipped with a set of dust removal components.
箱体内以隔板分隔为多个通道,每个通道依次排列有多个花板,各花板上安装有成束排列的多条滤袋。The box is divided into multiple channels by partitions, and each channel is arranged with multiple flower plates in turn, and each flower plate is equipped with multiple filter bags arranged in bundles.
所说的进气喇叭口和出气喇叭口分别在箱体的两侧水平设置。Said air intake bell mouth and air outlet bell mouth are respectively arranged horizontally on both sides of the box body.
烟气进口喇叭口设有多孔气流板或条形气流板。The flue gas inlet bell mouth is provided with a porous air flow plate or a strip air flow plate.
所说的水平喷吹岔管包含3~4根岔管,每根岔管均装有多个喷嘴。Said horizontal injection branch pipe comprises 3 to 4 branch pipes, and each branch pipe is equipped with a plurality of nozzles.
旋转风管底部装有耐磨的支撑轴承。Wear-resistant support bearings are installed at the bottom of the rotating air duct.
滤袋的袋口呈扁圆形,每个花板上的滤袋均以袋口按圆周排列并固定在花板上。The mouth of the filter bag is oblate, and the filter bags on each flower board are arranged in a circle with the mouth of the bag and fixed on the flower board.
本实用新型袋式除尘器采用旋转的风管和水平喷吹岔管,即喷嘴在滤袋束的上方的位置是随水平岔管的旋转不断地变换的,从而其喷出的压缩空气能均匀地到达滤袋束的每个滤袋,将附着在袋外壁的灰尘吹落入灰斗;因此,每个花板上方只需设置一套清灰组件,即由一个脉冲阀控制的一个旋转风管及其配套的水平喷吹管,即能完成该花板上全部滤袋(可达上千条滤袋)的清灰操作,与目前同类除尘器数百个固定管式喷吹相比,设备大大简化,节省材料,而且安装维修方便。本袋式除尘器可在同一箱体内紧凑地设置多个花板及其对应的滤袋束,并采用大型脉冲阀,可设置加长滤袋,适应特大流量烟气的除尘,结构紧凑,而且低能耗,高效率,节省设备投资,降低除尘成本。The bag type dust collector of the utility model adopts a rotating air pipe and a horizontal blowing branch pipe, that is, the position of the nozzle above the filter bag bundle is continuously changed with the rotation of the horizontal branch pipe, so that the compressed air sprayed out can be uniform. It reaches each filter bag of the filter bag bundle, and blows the dust attached to the outer wall of the bag into the ash hopper; therefore, only one set of dust removal components is needed above each flower plate, that is, a rotary wind blower controlled by a pulse valve. The pipe and its matching horizontal blowing pipe can complete the cleaning operation of all the filter bags (up to thousands of filter bags) on the flower plate. It is greatly simplified, saves materials, and is convenient for installation and maintenance. This bag type dust collector can compactly set multiple flower plates and the corresponding filter bag bundles in the same box, and adopts a large pulse valve, which can be equipped with extended filter bags, which is suitable for dust removal of extremely large flow of flue gas. It has a compact structure and low energy consumption. Low power consumption, high efficiency, saving equipment investment and reducing dust removal costs.
附图说明Description of drawings
图1是本旋转式低压大气量脉冲袋式除尘器结构示意图。Figure 1 is a schematic diagram of the structure of the rotary low-pressure large-volume pulse bag filter.
图2是图1的A向视图。Fig. 2 is a view along the direction A of Fig. 1 .
图3是水平喷吹岔管结构示意图。Fig. 3 is a schematic diagram of the structure of the horizontal injection branch pipe.
图4是气流分布板示意图。Fig. 4 is a schematic diagram of the air distribution plate.
图中:1是支架,2是进气喇叭口,3是气流分布板,4是壳体,5是烟气室,6是净气室,7是灰斗,8是出气喇叭口,9是滤袋束,10是旋转风管,11是花板,12是储气罐,13是平台楼梯,14是顶部通风孔,15是超大型脉冲阀,16是水平喷吹岔管,17是喷嘴,18是旋转电机,19是减速机,20是支撑轴承,21是隔墙。In the figure: 1 is the bracket, 2 is the air inlet bell mouth, 3 is the air distribution plate, 4 is the shell, 5 is the flue gas chamber, 6 is the clean air chamber, 7 is the ash hopper, 8 is the air outlet bell mouth, 9 is Filter bag bundle, 10 is the rotating air duct, 11 is the flower plate, 12 is the air storage tank, 13 is the platform stairs, 14 is the top ventilation hole, 15 is the super large pulse valve, 16 is the horizontal injection branch pipe, 17 is the nozzle , 18 is a rotating electrical machine, 19 is a speed reducer, 20 is a support bearing, and 21 is a partition wall.
具体实施方式Detailed ways
本实施例的旋转式低压大气量脉冲袋式除尘器如图1所示,旋转风管10下端设水平喷吹岔管16,上端连接顶部储气罐12,储气罐12顶部安装超大型脉冲阀15。含尘气体进入进气喇叭口2,通过气流分布板3的合理分配,进入烟气室5;悬挂在花板11上的滤袋束9起过滤作用,将粉尘阻挡在滤袋外表面;需要对滤袋清灰时,启动电机18,在旋转电机18驱动下,旋转风管10和水平喷吹岔管16一同转动,喷嘴17随水平喷吹岔管16作圆周运动,储气罐12内的压缩空气通过置超大型脉冲阀15形成脉冲,脉冲气从喷嘴17吹入滤袋内,对圆周排列的滤袋吹气,使滤袋鼓胀变形,将附着在滤袋外侧的积灰吹落入灰斗7,除尘后的洁净烟气进入滤袋内,从袋口升至净气室6,从净气室6的出气喇叭口8排出除尘器,达到清灰的目的。压缩空气不断充入顶部储气罐12中,保存在储气罐内,等待下一次清灰。The rotary low-pressure large-volume pulse bag filter of this embodiment is shown in Figure 1. The lower end of the rotary air duct 10 is provided with a horizontal
图2表示箱体4内由隔墙21分隔成两个通道,每个通道顶部排列有多个花板11,滤袋以扁圆形袋口依次呈圆周排列固定在花板11(图中袋口的排列省略)上。两通道隔开,便于在线隔离检修。图2还表示每个花板11的上方设有水平喷吹岔管16,本例中,每个水平喷吹岔管含有3根岔管。Figure 2 shows that the inside of the box body 4 is divided into two channels by a
图1和图2表示大型袋式除尘器设有平台楼梯13,操作人员通过平台楼梯13才能到达袋式除尘器设备的顶部。Figures 1 and 2 show that the large bag filter is provided with a
图3所示的是水平喷吹岔管,每个水平旋转风管设四支旋臂,每支悬臂上有多个喷嘴,随风管10旋转喷吹,一次可至少清灰50条滤袋。Figure 3 shows the horizontal blowing branch pipe, each horizontal rotating air pipe is equipped with four arms, and each cantilever has multiple nozzles, which rotate and spray with the air pipe 10, and at least 50 filter bags can be cleaned at one time .
图4所示的是烟气进气口喇叭口2设置的气流分布板3,可根据不同工况,通过实验设计出一定开孔率或间隙率的多孔板或条形板。Figure 4 shows the
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010200227309U CN201664549U (en) | 2010-01-07 | 2010-01-07 | Rotary low pressure air volume pulse bag filter |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010200227309U CN201664549U (en) | 2010-01-07 | 2010-01-07 | Rotary low pressure air volume pulse bag filter |
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| CN201664549U true CN201664549U (en) | 2010-12-08 |
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| CN2010200227309U Expired - Lifetime CN201664549U (en) | 2010-01-07 | 2010-01-07 | Rotary low pressure air volume pulse bag filter |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103894288A (en) * | 2014-03-26 | 2014-07-02 | 李连清 | Cavity-separated type aerosol capturing device |
| CN114028876A (en) * | 2021-12-18 | 2022-02-11 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary-spraying bag-type dust collector of circulating fluidized bed boiler |
| CN114754596A (en) * | 2022-03-09 | 2022-07-15 | 金川集团股份有限公司 | A kind of treatment method and device of anode slime feeding flue gas |
| CN117357980A (en) * | 2023-10-07 | 2024-01-09 | 华南理工大学 | A rotatable multi-branch backflush nozzle |
| CN118615798A (en) * | 2024-06-07 | 2024-09-10 | 常州市科健电力设备有限公司 | A pulse dust collector |
-
2010
- 2010-01-07 CN CN2010200227309U patent/CN201664549U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103894288A (en) * | 2014-03-26 | 2014-07-02 | 李连清 | Cavity-separated type aerosol capturing device |
| CN114028876A (en) * | 2021-12-18 | 2022-02-11 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary-spraying bag-type dust collector of circulating fluidized bed boiler |
| CN114028876B (en) * | 2021-12-18 | 2022-07-05 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary spraying cloth bag dust remover for circulating fluidized bed boiler |
| CN114754596A (en) * | 2022-03-09 | 2022-07-15 | 金川集团股份有限公司 | A kind of treatment method and device of anode slime feeding flue gas |
| CN117357980A (en) * | 2023-10-07 | 2024-01-09 | 华南理工大学 | A rotatable multi-branch backflush nozzle |
| CN118615798A (en) * | 2024-06-07 | 2024-09-10 | 常州市科健电力设备有限公司 | A pulse dust collector |
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Granted publication date: 20101208 |
