CN101036846A - Granular-layer dust precipitator - Google Patents
Granular-layer dust precipitator Download PDFInfo
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- CN101036846A CN101036846A CN 200710067109 CN200710067109A CN101036846A CN 101036846 A CN101036846 A CN 101036846A CN 200710067109 CN200710067109 CN 200710067109 CN 200710067109 A CN200710067109 A CN 200710067109A CN 101036846 A CN101036846 A CN 101036846A
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- dust precipitator
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- 239000000428 dust Substances 0.000 title claims abstract description 48
- 239000012716 precipitator Substances 0.000 title claims 11
- 238000009826 distribution Methods 0.000 claims abstract description 16
- 238000009423 ventilation Methods 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 3
- 230000000740 bleeding effect Effects 0.000 claims 3
- 230000008676 import Effects 0.000 claims 3
- 239000001301 oxygen Substances 0.000 claims 3
- 229910052760 oxygen Inorganic materials 0.000 claims 3
- 210000000498 stratum granulosum Anatomy 0.000 claims 3
- 239000002245 particle Substances 0.000 abstract description 14
- 238000001914 filtration Methods 0.000 abstract description 7
- 238000007664 blowing Methods 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
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- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
本发明公开了一种颗粒床过滤除尘器,包括外壳体和沿高度方向设置在外壳体内的至少一层过滤装置,外壳体的上部设置有含尘气进口,外壳体的下端设置有粉尘出口,过滤装置设置有独立的气体换向装置,气体换向装置上连接有净气总管和反吹气总管,特点是过滤装置包括至少一个过滤单元,过滤单元包括内壳体,内壳体上设置有通气口和通气管,内壳体内设置有颗粒层和布风板,通气口设置在颗粒层的上方,通气管设置在颗粒层的下方,通气管横向穿出外壳体与气体换向装置连接;优点是在过滤除尘时,内壳体被热气流包围,内壳体各部分热胀冷缩均匀,抗热变形性能好,使该除尘器能够用于高温及温度多变场合,适用范围广。
The invention discloses a particle bed filter and dust remover, which comprises an outer shell and at least one layer of filtering device arranged in the outer shell along the height direction, the upper part of the outer shell is provided with a dust-containing gas inlet, and the lower end of the outer shell is provided with a dust outlet. The filter device is equipped with an independent gas reversing device, and the gas reversing device is connected with a main pipe for cleaning gas and a main pipe for blowing back gas. Air vent and air pipe, the inner casing is provided with a granular layer and an air distribution plate, the air vent is arranged above the granular layer, the air pipe is arranged below the granular layer, and the air pipe passes through the outer casing laterally to connect with the gas reversing device; advantages When filtering and removing dust, the inner casing is surrounded by hot air flow, and each part of the inner casing expands and contracts evenly, and has good thermal deformation resistance, so that the dust collector can be used in high temperature and variable temperature occasions, and has a wide range of applications.
Description
技术领域technical field
本发明涉及一种除尘装置,尤其是涉及一种颗粒床过滤除尘器。The invention relates to a dust removal device, in particular to a particle bed filter dust remover.
背景技术Background technique
随着社会经济的发展,工业发展也越来越迅速,但是在工业生产中带来的粉尘也很多,这些粉尘主要存在于气体中,因此就需要设置相应的除尘装置。颗粒床过滤除尘装置因可以采用耐高温的滤料,如石英砂等,在高温气体除尘领域有独特优越性。但传统的颗粒床过滤除尘装置在反吹清灰时需要借助耙子及传动机构,而且清灰效果不好,工作效率不高。With the development of social economy, the industrial development is becoming more and more rapid, but there is also a lot of dust brought in by industrial production. These dusts mainly exist in the gas, so it is necessary to install corresponding dust removal devices. The particle bed filter dust removal device has unique advantages in the field of high temperature gas dust removal because it can use high temperature resistant filter materials, such as quartz sand. However, the traditional particle bed filter and dust removal device needs to use a rake and a transmission mechanism when blowing back to remove dust, and the dust removal effect is not good, and the work efficiency is not high.
专利号为ZL88201515.X的实用新型专利说明书中公开了一种燃劣质煤锅炉电颗粒层除尘装置,它是由沸腾反吹清灰颗粒层除尘器的沉降室内安装预荷电装置和尘气分流装置组成,该装置取消了传统的耙子和传动机构,结构比较简单,能干法、高效、低阻收集燃劣质煤锅炉排出的烟尘,但是这种装置由于结构上的原因使支承滤料的布风板受热不均,易变形而产生漏料和漏气,不能适用于高温或温度波动大的场合。The utility model patent specification with the patent No. ZL88201515.X discloses an electric particle layer dedusting device for boilers burning low-quality coal. The device is composed of the traditional rake and the transmission mechanism, and the structure is relatively simple. The plate is heated unevenly, and it is easy to deform to cause material leakage and air leakage, so it cannot be applied to occasions with high temperature or large temperature fluctuations.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种能适用于高温及温度波动大的场合的颗粒床过滤除尘器。The technical problem to be solved by the present invention is to provide a particle bed filter and dust collector applicable to occasions with high temperature and large temperature fluctuations.
本发明解决上述技术问题所采用的技术方案为:一种颗粒床过滤除尘器,包括外壳体和沿高度方向设置在所述的外壳体内的至少一层过滤装置,所述的外壳体的上部设置有含尘气进口,所述的外壳体的下端设置有粉尘出口,所述的过滤装置设置有独立的气体换向装置,所述的气体换向装置上连接有净气总管和反吹气总管,所述的过滤装置包括至少一个过滤单元,所述的过滤单元包括内壳体,所述的内壳体上设置有通气口和通气管,所述的内壳体内设置有颗粒层和布风板,所述的通气口设置在所述的颗粒层的上方,所述的通气管设置在所述的颗粒层的下方,所述的通气管横向穿出所述的外壳体与所述的气体换向装置连接。The technical solution adopted by the present invention to solve the above-mentioned technical problems is: a granular bed filter dust collector, comprising an outer casing and at least one layer of filtering devices arranged in the outer casing along the height direction, and the upper part of the outer casing is arranged There is a dust-containing gas inlet, the lower end of the outer shell is provided with a dust outlet, and the filter device is provided with an independent gas reversing device, and the gas reversing device is connected with a clean gas main pipe and a back-blowing air main pipe , the filter device includes at least one filter unit, the filter unit includes an inner casing, the inner casing is provided with a vent and a vent pipe, and the inner casing is provided with a particle layer and an air distribution plate , the air vent is arranged above the particle layer, the air pipe is arranged below the particle layer, and the air pipe passes through the outer casing laterally to communicate with the gas exchange Connect to the device.
所述的气体换向装置包括与所述的通气管连接的独立的换向阀,所述的换向阀分别与所述的净气总管和所述的反吹气总管连接。The gas reversing device includes an independent reversing valve connected with the ventilation pipe, and the reversing valve is respectively connected with the cleaning gas main pipe and the back blowing gas main pipe.
所述的气体换向装置包括换向阀和与所述的换向阀连接的通气支管,所述的换向阀与所述的净气总管和所述的反吹气总管连接,所述的通气管连接在所述的通气支管上。The gas reversing device includes a reversing valve and a ventilation branch pipe connected with the reversing valve, the reversing valve is connected with the main clean gas pipe and the blowback gas main pipe, the The ventilation pipe is connected to the ventilation branch pipe.
所述的内壳体中设置有预分布多孔板,所述的预分布多孔板设置在所述的布风板与所述的通气管之间。The inner casing is provided with a pre-distribution perforated plate, and the pre-distribution perforated plate is arranged between the air distribution plate and the air duct.
所述的过滤装置包括二个以上的过滤单元,所述的过滤单元在水平方向呈矩形分布或呈环形分布。The filtering device includes more than two filtering units, and the filtering units are distributed in a rectangular shape or in a circular shape in the horizontal direction.
所述的外壳体的壁面上设置有抽气口,所述的抽气口设置在所述的过滤装置与所述的粉尘出口之间。An air suction port is provided on the wall of the outer casing, and the air suction port is arranged between the filter device and the dust outlet.
所述的抽气口通过抽气和除尘装置与所述的含尘气进口连通。The air suction port communicates with the dust-containing gas inlet through an air suction and dust removal device.
所述的外壳体的横截面为圆形,所述的含尘气进口与所述的外壳体之间切向连接。The cross section of the outer casing is circular, and the dust-laden gas inlet is connected tangentially to the outer casing.
所述的内壳体的横截面为圆形或扇形或梯形。The cross-section of the inner casing is circular, fan-shaped or trapezoidal.
所述的内壳体的横截面为方形,所述的外壳体的横截面为方形。The cross section of the inner casing is square, and the cross section of the outer casing is square.
与现有技术相比,本发明的优点在于在过滤除尘时,内壳体被热气流包围,内壳体各部分热胀冷缩均匀,抗热变形性能好,使该除尘器能够用于高温及温度多变场合,适用范围广;又由于设置有至少一层过滤装置,且每个过滤装置都通过独立的气体换向装置分别与净气总管和反吹气总管连接,使各颗粒层独自清灰,且自上而下逐层流化清灰,粉尘逐层向下传输,清灰效果好;又由于含尘气进口切向引入外壳体,在离心力作用下得到预除尘,减轻颗粒层的过滤负荷,而且在外壳体的壁面上设置有抽气口,可将从颗粒层清理出来的粉尘抽出过滤器。Compared with the prior art, the present invention has the advantage that when filtering and removing dust, the inner casing is surrounded by hot air flow, each part of the inner casing expands with heat and contracts with cold, and has good thermal deformation resistance, so that the dust collector can be used in high temperature It has a wide range of applications and occasions with variable temperatures; and because at least one filter device is provided, and each filter device is connected to the main clean gas pipe and the back blow gas main pipe through an independent gas reversing device, so that each particle layer can be separated by itself. Dust removal, and from top to bottom, layer by layer fluidization, the dust is transmitted layer by layer downward, and the effect of dust removal is good; and because the dusty gas inlet is tangentially introduced into the outer shell, pre-dust removal is obtained under the action of centrifugal force, reducing the particle layer The filter load, and there is an air suction port on the wall of the outer casing, which can suck the dust cleaned from the particle layer out of the filter.
附图说明Description of drawings
图1为本发明的剖面结构示意图;Fig. 1 is the sectional structure schematic diagram of the present invention;
图2为本发明的不同方向的剖面示意图;Fig. 2 is a schematic cross-sectional view of different directions of the present invention;
图3为本发明的实施例一的剖视图;Fig. 3 is the sectional view of embodiment one of the present invention;
图4为本发明的实施例二的剖视图;Fig. 4 is the sectional view of embodiment two of the present invention;
图5为本发明的含尘进气口与外壳体的连接示意图。Fig. 5 is a schematic diagram of the connection between the dust-containing air inlet and the outer shell of the present invention.
具体实施方式Detailed ways
以下结合附图实施例对本发明作进一步详细描述。The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments.
实施例一:如图所示,一种颗粒床过滤除尘器,包括外壳体1,外壳体1的上部设置有含尘气进口2,外壳体1的下端设置有粉尘出口3,外壳体1的内部沿高度方向的每一层上并列设置有两个独立的内壳体4,共设置有三层,内壳体4的内部设置有颗粒层5和设置在颗粒层5下方的布风板6,布风板6的下方设置有预分布多孔板7,内壳体4上设置有通气口8和通气管9,通气口8设置在颗粒层5的上方,通气管9设置在预分布多孔板7的下方并横向穿出外壳体1独立连接有换向阀10,换向阀10分别与净气总管11和反吹气总管12连接,外壳体1的壁面上设置有抽气口13,抽气口13设置在最后一层内壳体4与粉尘出口3之间,外壳体1上还设置有维修孔14,且内壳体4与外壳体1的横截面均为方形。Embodiment 1: As shown in the figure, a particle bed filter and dust collector includes an
实施例二:如图所示,其它结构同实施例一,不同之处在于同一层上并列的两个通气管9均与通气支管15连接,通气支管15上连接有独立的换向阀10,换向阀10分别与净气总管11和反吹气总管12连接。Embodiment two: as shown in the figure, other structures are the same as embodiment one, and the difference is that the two
除上述所述结构之外,外壳体1内部每一层内壳体4的数量可以为三个,也可以为四个,但不能少于一个;当每一层内壳体4的数量在两个以上时,内壳体4的排列方式可以是矩形分布,也可以是环形分布(内壳体4的横截面为扇形或梯形时);外壳体1内部设置有内壳体4的层的数量可以为两层,也可以为四层,但同样不能少于一层;抽气口13还可以通过抽气和除尘装置与含尘气进口2连通;此外,外壳体1的横截面为圆形时,内壳体4的横截面还可以为圆形、扇形或者梯形,而且外壳体1和含尘气进口2还可以设置成切向连接。In addition to the above-mentioned structure, the number of
Claims (10)
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Cited By (12)
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CN101934177A (en) * | 2010-09-14 | 2011-01-05 | 宁波大学 | Granular bed gas filtration and purification device |
CN101940862A (en) * | 2010-09-14 | 2011-01-12 | 宁波大学 | Gas filtering and purifying device |
CN101940863A (en) * | 2010-09-14 | 2011-01-12 | 宁波大学 | Granular-bed gas filtration and purification device |
CN104740969A (en) * | 2015-03-24 | 2015-07-01 | 山东神华山大能源环境有限公司 | Boiling type granular layer filter dust separator |
CN104874242A (en) * | 2015-05-29 | 2015-09-02 | 扬中市第一蝶阀厂有限公司 | Granular layer filtration device based dust cleaning system |
CN105670709A (en) * | 2016-03-29 | 2016-06-15 | 新疆广汇中化能源技术开发有限公司 | Raw gas purification plant |
CN106422591A (en) * | 2016-08-31 | 2017-02-22 | 宁波大学 | Particle bed filtering and dust removing device |
CN106975305A (en) * | 2017-04-18 | 2017-07-25 | 宁波大学 | A kind of Bed Filtration dust pelletizing system |
CN107158942A (en) * | 2017-06-30 | 2017-09-15 | 合肥天翔环境工程有限公司 | A kind of sintering furnace flue-gas dust-removing and desulfurization system |
CN107321090A (en) * | 2017-08-21 | 2017-11-07 | 江阴远帆环保科技有限公司 | Hot precipitator |
CN108211535A (en) * | 2017-12-29 | 2018-06-29 | 新疆广汇煤炭清洁炼化有限责任公司 | Deduster |
CN112627957A (en) * | 2019-09-24 | 2021-04-09 | 天纳克(苏州)排放系统有限公司 | Tail gas aftertreatment encapsulation |
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CN1305550C (en) * | 2004-11-22 | 2007-03-21 | 宁波大学 | Granular bed gas purifying device and its method |
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2007
- 2007-01-31 CN CNB2007100671097A patent/CN100446837C/en not_active Expired - Fee Related
Cited By (17)
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CN101940862A (en) * | 2010-09-14 | 2011-01-12 | 宁波大学 | Gas filtering and purifying device |
CN101940863A (en) * | 2010-09-14 | 2011-01-12 | 宁波大学 | Granular-bed gas filtration and purification device |
CN101940862B (en) * | 2010-09-14 | 2012-06-06 | 宁波大学 | Gas filtering and purifying device |
CN101940863B (en) * | 2010-09-14 | 2012-08-22 | 宁波大学 | Granular-bed gas filtration and purification device |
CN101934177A (en) * | 2010-09-14 | 2011-01-05 | 宁波大学 | Granular bed gas filtration and purification device |
CN104740969A (en) * | 2015-03-24 | 2015-07-01 | 山东神华山大能源环境有限公司 | Boiling type granular layer filter dust separator |
CN104874242A (en) * | 2015-05-29 | 2015-09-02 | 扬中市第一蝶阀厂有限公司 | Granular layer filtration device based dust cleaning system |
CN105670709B (en) * | 2016-03-29 | 2020-02-18 | 新疆广汇煤炭清洁炼化有限责任公司 | Raw coke oven gas purification device |
CN105670709A (en) * | 2016-03-29 | 2016-06-15 | 新疆广汇中化能源技术开发有限公司 | Raw gas purification plant |
CN106422591A (en) * | 2016-08-31 | 2017-02-22 | 宁波大学 | Particle bed filtering and dust removing device |
CN106422591B (en) * | 2016-08-31 | 2018-09-11 | 宁波大学 | A kind of Bed Filtration dust-extraction unit |
CN106975305A (en) * | 2017-04-18 | 2017-07-25 | 宁波大学 | A kind of Bed Filtration dust pelletizing system |
CN106975305B (en) * | 2017-04-18 | 2022-07-15 | 宁波大学 | A particle bed filter and dust removal system |
CN107158942A (en) * | 2017-06-30 | 2017-09-15 | 合肥天翔环境工程有限公司 | A kind of sintering furnace flue-gas dust-removing and desulfurization system |
CN107321090A (en) * | 2017-08-21 | 2017-11-07 | 江阴远帆环保科技有限公司 | Hot precipitator |
CN108211535A (en) * | 2017-12-29 | 2018-06-29 | 新疆广汇煤炭清洁炼化有限责任公司 | Deduster |
CN112627957A (en) * | 2019-09-24 | 2021-04-09 | 天纳克(苏州)排放系统有限公司 | Tail gas aftertreatment encapsulation |
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