CN201632155U - Long bag low pressure bag filter - Google Patents
Long bag low pressure bag filter Download PDFInfo
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- CN201632155U CN201632155U CN2010201594362U CN201020159436U CN201632155U CN 201632155 U CN201632155 U CN 201632155U CN 2010201594362 U CN2010201594362 U CN 2010201594362U CN 201020159436 U CN201020159436 U CN 201020159436U CN 201632155 U CN201632155 U CN 201632155U
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- 238000007599 discharging Methods 0.000 claims 3
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 230000003111 delayed effect Effects 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 59
- 238000007664 blowing Methods 0.000 abstract description 10
- 238000004140 cleaning Methods 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 239000004568 cement Substances 0.000 description 5
- 238000001914 filtration Methods 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003365 glass fiber Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- -1 electric power Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000126 substance Substances 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
一种长袋低压袋式除尘器,涉及一种环保除尘设备,除尘器的箱体包括上部箱体、中部箱体和灰斗,灰斗设置在中部箱体的下部,在上部箱体和中部箱体构成的箱体空间内设置多个袋室,袋室内放置滤袋,顶部开有袋口,还包括设置在除尘器箱体内的清灰装置、卸灰装置和控制系统,控制系统控制清灰装置和卸灰装置的开启和关闭;中部箱体和灰斗的连接处制有进风孔,上部箱体的顶部设置出风口和排气孔,排气孔、袋室的袋口和出风口同引风机相连,将净化后气体排入大气,风尘被阻留在滤袋外部;清灰装置和卸灰装置由提升阀、电磁脉冲阀和喷吹管构成,分别和控制系统之间电连接。有益效果是除尘器采用离线或在线逐袋喷吹清灰方式,清灰效果好、除尘效率高、排放浓度底,同时还具有处理风量大、运行可靠、维护方便、结构合理、运行阻力低、占地面积小。
A long-bag low-pressure bag-type dust collector, which relates to an environment-friendly dust removal equipment. The box body of the dust collector includes an upper box body, a middle box body, and an ash hopper. There are multiple bag rooms in the box space formed by the box. Filter bags are placed in the bag rooms, and the top has a bag opening. It also includes ash cleaning device, ash unloading device and control system installed in the dust collector box. The control system controls the cleaning. The opening and closing of the ash device and the ash unloading device; the connection between the middle box and the ash hopper is made with an air inlet, and the top of the upper box is equipped with an air outlet and an exhaust hole. The tuyere is connected with the induced draft fan, and the purified gas is discharged into the atmosphere, and the wind dust is blocked outside the filter bag; the dust cleaning device and the dust unloading device are composed of a poppet valve, an electromagnetic pulse valve and a blowing pipe, which are respectively electrically connected to the control system . The beneficial effect is that the dust collector adopts the off-line or on-line bag-by-bag dust cleaning method, which has good dust removal effect, high dust removal efficiency, and low emission concentration. It also has large processing air volume, reliable operation, convenient maintenance, reasonable structure, and low running resistance. Small footprint.
Description
技术领域technical field
本实用新型涉及一种环保除尘设备,主要用于处理大量的含尘气流进行粉尘捕集的长袋低压袋式除尘器。The utility model relates to an environment-friendly dedusting device, which is mainly used for a long-bag low-pressure bag-type deduster for processing a large amount of dust-laden airflow for dust collection.
背景技术Background technique
我国是水泥生产和消费大国,水泥产量占世界的一半以上,随着我国水泥行业的逐步调整,上大改小的方针的不断落实,一大批落后的工艺设备逐步淘汰,大型化,集约化成为发展方向。水泥工业的粉尘排放,是造成大气污染的一个重要原因。虽然,目前在水泥行业的窑头,窑尾等粉尘排放点,通常采用玻纤布袋除尘器来处理大风量的粉尘捕集,但由于玻纤布袋除尘器过滤风速较低,一般为0.4~0.5m/s,造成整个除尘器体积大、占地面积大,投资高,加上其采用反吹缩袋清灰,给除尘器本身带来额外负荷,也影响滤袋使用寿命,限制了其自身的发展。在另一方面,如果采用高压脉冲袋除尘器,虽然有良好的效果,但因其需要的动能大,能耗较高,不利于企业的节能降耗。因此,研究一种采用低压脉冲清灰、长袋结构的袋式除尘器非常必要。my country is a big country in cement production and consumption, and its cement output accounts for more than half of the world. With the gradual adjustment of my country's cement industry and the continuous implementation of the policy of changing from large to small, a large number of backward process equipment are gradually eliminated, and large-scale and intensified become Direction of development. Dust emission from the cement industry is an important cause of air pollution. Although at present, at the kiln head, kiln tail and other dust discharge points in the cement industry, glass fiber bag dust collectors are usually used to deal with large air volume dust collection, but due to the low filtration wind speed of glass fiber bag dust collectors, generally 0.4 to 0.5 m/s, resulting in large volume, large floor space and high investment of the entire dust collector. In addition, it uses back blowing shrink bag to clean dust, which brings extra load to the dust collector itself, and also affects the service life of the filter bag, which limits its own development of. On the other hand, if the high-voltage pulse bag filter is used, although it has a good effect, it is not conducive to the energy saving and consumption reduction of the enterprise because of the large kinetic energy required and high energy consumption. Therefore, it is very necessary to study a bag filter with low-pressure pulse cleaning and long bag structure.
实用新型内容Utility model content
本实用新型所要解决的技术问题在于提供一种在脉冲喷吹(Jet Puise)除尘技术的基础上,为满足大风量烟气需要的长袋低压袋式除尘器。The technical problem to be solved by the utility model is to provide a long-bag low-pressure bag-type dust collector based on the pulse jet (Jet Puise) dust removal technology to meet the needs of large-volume flue gas.
本实用新型为解决技术问题采用的技术方案是,The technical scheme that the utility model adopts for solving technical problems is,
一种长袋低压袋式除尘器,其特征在于:所述除尘器的箱体包括上部箱体、中部箱体和灰斗,灰斗设置在中部箱体的下部,在上部箱体和中部箱体构成的箱体空间内设置多个袋室,袋室内放置滤袋,顶部开有袋口,在所述中部箱体和灰斗的连接处制有进风孔,所述上部箱体的顶部设置出风口和排气孔,所述排气孔、袋室的袋口和出风口同引风机相连,将净化后气体排入大气,风尘被阻留在滤袋外部。A long-bag low-pressure bag-type dust collector, characterized in that: the box of the dust collector includes an upper box, a middle box and an ash hopper, the ash hopper is arranged at the lower part of the middle box, and the upper box and the middle box A plurality of bag chambers are arranged in the box body space formed by the box body, and filter bags are placed in the bag rooms, and a bag opening is opened on the top. An air outlet and an air vent are arranged, and the air outlet, the bag mouth of the bag chamber and the air outlet are connected with the induced draft fan, and the purified gas is discharged into the atmosphere, and the dust is blocked outside the filter bag.
还包括设置在除尘器箱体内的清灰装置、卸灰装置和控制系统,控制系统控制清灰装置和卸灰装置的开启和关闭,所述清灰装置和卸灰装置由提升阀、电磁脉冲阀和喷吹管构成,分别和控制系统之间电连接,所述电磁脉冲阀和喷吹管之间也电连接。It also includes a dust removal device, a dust discharge device and a control system arranged in the dust collector box. The control system controls the opening and closing of the dust removal device and the dust discharge device. The dust removal device and the dust discharge device are controlled by a poppet valve, an electromagnetic pulse The valve and the blowing pipe are formed, and are respectively electrically connected to the control system, and the electromagnetic pulse valve is also electrically connected to the blowing pipe.
所述提升阀设置在每个袋室的上部,并和袋口相接成一起,用于关闭袋口,切断袋室中的过滤气流,电磁脉冲阀在压缩空气后经由喷吹管上的喷吹嘴向滤袋喷射。The poppet valve is arranged on the upper part of each bag chamber and is connected with the bag mouth to close the bag mouth and cut off the filtered air flow in the bag chamber. After the compressed air, the electromagnetic pulse valve blows The nozzle sprays into the filter bag.
所述喷吹管由无缝钢管制成。The blowing pipe is made of seamless steel pipe.
所述的控制系统为清灰控制器。The control system is a dust removal controller.
本实用新型的工作原理是含尘烟气由进风口经中部箱体的下部进入灰斗,部分较大的尘粒由于惯性碰撞、自然沉降等作用直接落入灰斗,其他尘粒随气体上升进入各个袋室,经滤袋过滤后,净化后的气体从滤袋内部经过袋口、排气孔、出风口由引风机排入大气,风尘被阻留在滤袋外面。随着过滤的不断进行,滤袋外面所附积的粉尘不断增加,从而导致除尘器本身的阻力也逐步升高,当阻力达到一定值时,清灰控制器发出信号,首先令一袋室的提升阀关闭以切断该室的过滤气流,然后打开电磁脉冲阀,压缩空气经气包、脉冲阀、喷吹管上的喷吹嘴以极短时间(0.2-0.3秒)向滤袋内喷射,压缩空气在滤袋内高速膨胀,使滤袋产生高频振动变形,再加上逆气流的作用,使滤袋外侧所附尘饼变形脱落。在充分考虑了粉尘的沉降时间(保证所脱落的粉尘能够有效的落入灰斗)后,该袋室提升阀门打开,此袋室恢复到过滤状态,而下一袋室则进入清灰状态,如此往复直到最后一个袋室清灰结束。The working principle of the utility model is that the dust-laden flue gas enters the ash hopper through the air inlet through the lower part of the middle box, and some larger dust particles fall directly into the ash hopper due to inertial collision, natural settlement, etc., and other dust particles rise with the gas. After entering each bag room, after being filtered by the filter bag, the purified gas is discharged into the atmosphere from the inside of the filter bag through the bag mouth, exhaust hole, and air outlet by the induced draft fan, and the dust is blocked outside the filter bag. As the filtration continues, the dust accumulated on the outside of the filter bag continues to increase, which leads to a gradual increase in the resistance of the dust collector itself. When the resistance reaches a certain value, the dust cleaning controller sends out a signal to firstly make the dust collector in a bag room The poppet valve is closed to cut off the filtered air flow in the chamber, then the electromagnetic pulse valve is opened, and the compressed air is sprayed into the filter bag in a very short time (0.2-0.3 seconds) through the air bag, the pulse valve, and the injection nozzle on the injection pipe, compressing The air expands at a high speed in the filter bag, which causes the filter bag to produce high-frequency vibration and deformation, and the effect of the reverse air flow causes the dust cake attached to the outside of the filter bag to deform and fall off. After fully considering the dust settling time (to ensure that the fallen dust can effectively fall into the ash hopper), the lifting valve of the bag room is opened, the bag room returns to the filtering state, and the next bag room enters the dust cleaning state. This goes on and on until the cleaning of the last baghouse is completed.
本实用新型具有的有益效果是除尘器采用离线或在线逐袋喷吹清灰方式,清灰效果好、除尘效率高、排放浓度底,同时还具有处理风量大、运行可靠、维护方便、结构合理、运行阻力低、占地面积小等优点,可广泛适用于冶金、钢铁、电力、化工、机械、建材等行业的大风量烟气净化。The beneficial effect of the utility model is that the dust remover adopts the off-line or on-line bag-by-bag blowing dust removal method, which has good dust removal effect, high dust removal efficiency, and low emission concentration. At the same time, it also has large processing air volume, reliable operation, convenient maintenance and reasonable structure. , low running resistance, small footprint, etc., can be widely used in large-volume flue gas purification in metallurgy, steel, electric power, chemical industry, machinery, building materials and other industries.
附图说明Description of drawings
图1是实用新型的整机结构示意图。Fig. 1 is the schematic diagram of the whole machine structure of the utility model.
图2是图1的侧面示意图;Fig. 2 is a schematic side view of Fig. 1;
图3是上部箱体顶部的结构示意图;Fig. 3 is a schematic structural view of the top of the upper box;
图4是图3的侧面示意图;Fig. 4 is a schematic side view of Fig. 3;
图5是图3中喷吹管结构示意图。Fig. 5 is a schematic diagram of the structure of the blowing pipe in Fig. 3 .
具体实施方式Detailed ways
为了使本实用新型实现的技术手段、创作特征、达成目的与功效易于明白了解,下面结合具体图示,进一步阐述本实用新型。In order to make the technical means, creative features, goals and effects achieved by the utility model easy to understand, the utility model will be further elaborated below in conjunction with specific illustrations.
如图1和图2所示,一种长袋低压袋式除尘器1,除尘器1外部的箱体包括上部箱体11、中部箱体12和灰斗13,灰斗13设置在中部箱体12的下部,在上部箱体11和中部箱体12构成的空间内分割成多个袋室,袋室内放置滤袋,顶部开有袋口(图中未示出),在中部箱体12和灰斗13的连接处制有进风孔14,上部箱体11的顶部安装出风口和排气孔,排气孔、袋室的袋口和出风口同引风机相连,将净化后气体排入大气,风尘被阻留在滤袋外部。As shown in Figure 1 and Figure 2, a long bag low-pressure
如图1、图3-5所示,还包括设置在除尘器1箱体内的清灰装置、卸灰装置和控制系统,控制系统控制清灰装置和卸灰装置的开启和关闭,控制系统为清灰控制器,清灰装置和卸灰装置由提升阀15、电磁脉冲阀和喷吹管16构成,电磁脉冲阀安装于上部箱体的内空间(图中未示出),提升阀15、电磁脉冲阀和喷吹管16分别和控制系统之间电连接,电磁脉冲阀和喷吹管16之间也电连接。As shown in Figure 1 and Figure 3-5, it also includes a dust removal device, an ash unloading device and a control system arranged in the
将每个提升阀15安装在每个袋室的上部,并和袋口相接成一起,用于关闭袋口,切断袋室中的过滤气流,电磁脉冲阀在压缩空气后经由喷吹管16上的喷吹嘴向滤袋喷射。压缩空气在滤袋内高速膨胀,使滤袋产生高频振动变形,再加上逆气流的作用,使滤袋外侧所附尘饼变形脱落,在粉尘的沉降充分的时候,保证所脱落的粉尘能够有效的落入灰斗,该袋室提升阀15打开,此袋室恢复到过滤状态,而下一袋室则进入清灰状态,如此往复直到最后一个袋室清灰结束,交替使用。Each
以上显示和描述了本实用新型的基本原理和主要特征和本实用新型的优点。本行业的技术人员应该了解,本实用新型不受上述实施例的限制,上述实施例和说明书中描述的只是说明本实用新型的原理,在不脱离本实用新型精神和范围的前提下,本实用新型还会有各种变化和改进,这些变化和改进都落入要求保护的本实用新型范围内。本实用新型要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present utility model and the advantages of the present utility model have been shown and described above. Those skilled in the art should understand that the utility model is not limited by the above-mentioned embodiments. The above-mentioned embodiments and descriptions only illustrate the principle of the utility model. Without departing from the spirit and scope of the utility model, the utility model The new model also has various changes and improvements, and these changes and improvements all fall within the scope of the claimed utility model. The scope of protection required by the utility model is defined by the appended claims and their equivalents.
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102350147A (en) * | 2011-07-06 | 2012-02-15 | 哈尔滨工业大学(威海) | Integrative adsorptive dust collection device |
CN102580417A (en) * | 2012-03-21 | 2012-07-18 | 泉州中洲环保技术开发有限公司 | High-temperature smoke bag type dust remover of submerged arc furnace, dust removing process and dust removing system |
CN103285674A (en) * | 2013-05-22 | 2013-09-11 | 江苏新鹏重型机电制造有限公司 | High-temperature low-pressure long-bag pulse dust remover |
CN103912944A (en) * | 2014-04-04 | 2014-07-09 | 安徽省含山县天顺环保设备有限公司 | Air purification bag |
CN104400669A (en) * | 2014-11-20 | 2015-03-11 | 盐城市丰特铸造机械有限公司 | Dust removing device for stone shot blasting |
WO2015032018A1 (en) * | 2013-09-04 | 2015-03-12 | 江苏绿叶机械有限公司 | Compartmentalized dust remover |
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CN106268135A (en) * | 2016-08-29 | 2017-01-04 | 合肥合意环保科技工程有限公司 | One faces formula pulse bag-type dust-removing device directly |
CN109603337A (en) * | 2019-02-20 | 2019-04-12 | 北京博电兴源节能科技有限公司 | A kind of promotion door panel-type air-flow bag type dust-remover |
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Cited By (17)
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CN102350147B (en) * | 2011-07-06 | 2013-08-14 | 哈尔滨工业大学(威海) | Integrative adsorptive dust collection device |
CN102350147A (en) * | 2011-07-06 | 2012-02-15 | 哈尔滨工业大学(威海) | Integrative adsorptive dust collection device |
CN102580417A (en) * | 2012-03-21 | 2012-07-18 | 泉州中洲环保技术开发有限公司 | High-temperature smoke bag type dust remover of submerged arc furnace, dust removing process and dust removing system |
CN103285674A (en) * | 2013-05-22 | 2013-09-11 | 江苏新鹏重型机电制造有限公司 | High-temperature low-pressure long-bag pulse dust remover |
WO2015032018A1 (en) * | 2013-09-04 | 2015-03-12 | 江苏绿叶机械有限公司 | Compartmentalized dust remover |
CN103912944A (en) * | 2014-04-04 | 2014-07-09 | 安徽省含山县天顺环保设备有限公司 | Air purification bag |
CN104400669B (en) * | 2014-11-20 | 2017-02-01 | 盐城市丰特铸造机械有限公司 | Dust removing device for stone shot blasting |
CN104400669A (en) * | 2014-11-20 | 2015-03-11 | 盐城市丰特铸造机械有限公司 | Dust removing device for stone shot blasting |
CN105817085A (en) * | 2016-06-16 | 2016-08-03 | 石鸿娟 | Energy-saving dust removing device |
CN106215557A (en) * | 2016-08-29 | 2016-12-14 | 合肥合意环保科技工程有限公司 | A kind of dehydrator frosting resistance glass fiber bag type cleaner |
CN106268135A (en) * | 2016-08-29 | 2017-01-04 | 合肥合意环保科技工程有限公司 | One faces formula pulse bag-type dust-removing device directly |
CN106215559A (en) * | 2016-08-29 | 2016-12-14 | 合肥合意环保科技工程有限公司 | A kind of long bag and low pulse bag-type dust collecting equipment |
CN109603337A (en) * | 2019-02-20 | 2019-04-12 | 北京博电兴源节能科技有限公司 | A kind of promotion door panel-type air-flow bag type dust-remover |
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CN109603338B (en) * | 2019-02-20 | 2021-03-30 | 北京博电兴源节能科技有限公司 | Multi-valve collaborative type air flow ash removal bag type dust collector |
CN109603337B (en) * | 2019-02-20 | 2021-03-30 | 北京博电兴源节能科技有限公司 | Lifting door plate type air flow ash removal bag type dust collector |
CN111974102A (en) * | 2020-07-02 | 2020-11-24 | 黄山天之都环境科技发展有限公司 | Bag collector high in clouds online monitored control system |
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