CN103263816B - Air box-bag type dust collector integrated with high efficiency cyclone dust collection - Google Patents

Air box-bag type dust collector integrated with high efficiency cyclone dust collection Download PDF

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CN103263816B
CN103263816B CN201310157707.9A CN201310157707A CN103263816B CN 103263816 B CN103263816 B CN 103263816B CN 201310157707 A CN201310157707 A CN 201310157707A CN 103263816 B CN103263816 B CN 103263816B
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cyclone
gravity
dust collection
face plate
dust removal
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CN103263816A (en
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赵红霞
仝军锋
侯洪海
李妙玲
常家东
崔钦华
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Luoyang Institute of Science and Technology
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Abstract

一种集高效旋风收尘的气箱式袋式收尘器,包括带有进风口、洁净气体出口的壳体,在壳体的空腔内设有袋式收尘部分和重力旋风除尘部分,重力旋风除尘部分和袋式收尘部分串联连接,含尘气体通过进风口进入壳体内并依次经过重力旋风除尘部分、袋式收尘部分处理后排出,在所述的重力旋风除尘部分和袋式收尘部分上均设有出灰口,该装置通过对重力旋风除尘部分进行改进,并将内部空间合理分割成重力沉降室和旋风分离室,有效对含尘气体多级处理,保证除尘效果,经重力旋风除尘部分处理后的气体经其出风口进入袋式除尘部分进行再次除尘,整个设备具有收尘效率低,运行费用小,占地面积小的优点。

An air box-type bag dust collector with high-efficiency cyclone dust collection, including a housing with an air inlet and a clean gas outlet, and a bag-type dust collection part and a gravity cyclone dust removal part are arranged in the cavity of the housing. The gravity cyclone dust removal part and the bag dust collection part are connected in series, and the dust-containing gas enters the housing through the air inlet and is discharged after being processed by the gravity cyclone dust removal part and the bag dust collection part. There are ash outlets on the dust collection part. The device improves the gravity cyclone dust removal part and divides the internal space into a gravity settling chamber and a cyclone separation chamber reasonably, effectively treating the dusty gas in multiple stages to ensure the dust removal effect. The gas processed by the gravity cyclone dust removal part enters the bag dust removal part through its air outlet for further dust removal. The whole equipment has the advantages of low dust collection efficiency, low operating cost and small footprint.

Description

一种集高效旋风收尘的气箱式袋式收尘器An air-box bag-type dust collector with high-efficiency cyclone dust collection

技术领域 technical field

本发明涉及一种袋式收尘设备,具体的说是一种集高效旋风收尘的气箱式袋式收尘器。 The invention relates to a bag type dust collecting device, in particular to an air box type bag type dust collector which collects high-efficiency cyclone dust collection.

背景技术 Background technique

目前,市场上的除尘器已经是比较成熟的技术,主要有旋风除尘、重力除尘、袋式收尘、电除尘等等,然而基于重力沉降、旋风除尘并结合袋式除尘的设备并不多,而且大多装置均因为结构复杂、处理风量小,因此急需要提供一种分离效果好、能耗低的集高效旋风收法的PPF气箱式袋式收尘器。 At present, the dust collectors on the market are relatively mature technologies, mainly including cyclone dust removal, gravity dust removal, bag dust collection, electric dust removal, etc. However, there are not many equipment based on gravity sedimentation, cyclone dust removal and bag dust removal. Moreover, most of the devices are complex in structure and small in handling air volume, so there is an urgent need to provide a PPF air box bag type dust collector with good separation effect and low energy consumption, which integrates high-efficiency cyclone collection.

发明内容 Contents of the invention

为解决上述技术问题,本发明提供一种集高效旋风收尘的气箱式袋式收尘器,该装置为重力沉降、旋风除尘并结合气箱式袋式除尘一体化结构设计,并且将重力沉降室通过旋风子上花板、旋风子下花板和阻尼板阻隔成一级重力沉降室和二级重力沉降室,并将多个倾斜设置旋风子分布在一级重力沉降室内,该结构有效集合重力沉降、旋风收尘,所以从原理上讲,是重力沉降、旋风收尘、重力沉降三级串联,所以收尘效率高,其次又因单个旋风子尺寸小,旋风收尘效率高,总收尘效率提高。该结构另外一优点是多个旋风子并联,并同处一壳体内,所以处理风量可以随旋风子数量个数而增加。且系统散热面积减少,使系统散热减少,不会因系统散热问题影响袋式收尘的可靠运行。带有多个旋风子的高效旋风收尘从结构上讲可以满足任何风量的含尘气体的处理需求,而气箱式袋式收尘器也可能通过滤袋箱的并联组合,满足任何风量含尘气体的处理需求。因此,整个设备具有处理风量大,收尘效率高,运行费用小,占地面积小的优点。 In order to solve the above technical problems, the present invention provides an air box bag type dust collector with high efficiency cyclone dust collection. The settling chamber is separated into a first-level gravity settling chamber and a second-level gravity settling chamber by the upper flower plate of the cyclone, the lower flower plate of the cyclone and the damping plate, and multiple inclined cyclones are distributed in the first-level gravity settling room. Gravity sedimentation and cyclone dust collection, so in principle, it is a three-stage series connection of gravity sedimentation, cyclone dust collection, and gravity sedimentation, so the dust collection efficiency is high. Secondly, because of the small size of a single cyclone, the cyclone dust collection efficiency is high, and the total collection Increased dust efficiency. Another advantage of this structure is that multiple cyclones are connected in parallel and are in the same casing, so the air volume can be increased with the number of cyclones. And the system heat dissipation area is reduced, so that the system heat dissipation is reduced, and the reliable operation of the bag dust collector will not be affected by the system heat dissipation problem. The high-efficiency cyclone dust collection with multiple cyclones can meet the processing requirements of dusty gas with any air volume in terms of structure, and the air box bag filter can also meet the requirements of any air volume and content through the parallel combination of filter bag boxes. Dust gas treatment needs. Therefore, the whole equipment has the advantages of large air volume, high dust collection efficiency, low operating cost and small floor space.

本发明所采用的技术方案是:一种集高效旋风收尘的气箱式袋式收尘器,包括带有进风口、洁净气体出口的壳体,在壳体的空腔内设有袋式收尘部分和重力旋风除尘部分,重力旋风除尘部分和袋式收尘部分串联连接,含尘气体通过进风口进入壳体内并依次经过重力旋风除尘部分、袋式收尘部分处理后排出,在所述的重力旋风除尘部分和袋式收尘部分上均设有出灰口,所述的重力旋风除尘部分包括重力沉降室和设置在重力沉降室内的旋风子,所述的重力沉降室由旋风子上花板、旋风子下花板和阻尼板将重力沉降室内的空腔分割成一级重力沉降室和二级重力沉降室,进风口与所述的一级重力沉降室相连通;所述一级重力沉降室由旋风子上花板、旋风子下花板和阻尼板包围而成,其中,旋风子上花板、旋风子下花板分别与水平面呈锐角设置,阻尼板设置在远离进风口的一侧,并在所述阻尼板开设有重力沉降粉尘出口; The technical solution adopted in the present invention is: an air box bag type dust collector with high-efficiency cyclone dust collection, including a housing with an air inlet and a clean gas outlet, and a bag type dust collector is provided in the cavity of the housing. The dust collection part and the gravity cyclone dust removal part, the gravity cyclone dust removal part and the bag dust collection part are connected in series. Both the gravity cyclone dust removal part and the bag dust collection part are provided with ash outlets, the gravity cyclone dust removal part includes a gravity settling chamber and a cyclone arranged in the gravity settling chamber, and the gravity settling chamber consists of a cyclone The upper flower plate, the lower flower plate of the cyclone and the damping plate divide the cavity in the gravity settling chamber into a first-level gravity settling room and a second-level gravity settling room, and the air inlet communicates with the first-level gravity settling room; The gravity settling chamber is surrounded by the upper flower plate of the cyclone, the lower flower plate of the cyclone and the damping plate. Among them, the upper flower plate of the cyclone and the lower flower plate of the cyclone are respectively set at an acute angle with the horizontal plane, and the damping plate is set far away from the air inlet. One side, and a gravity settling dust outlet is opened on the damping plate;

所述旋风子设置在一级重力沉降室内,旋风子内部的空间为旋风分离室,旋风子固定连接在旋风子上花板和旋风子下花板之间,旋风子的中轴线分别垂直于旋风子上花板和旋风子下花板,旋风子的含尘气体进口位于一级重力沉降室内,旋风子上端的分离气体出口和下端的排灰尘口均与二级重力沉降室相连通。 The cyclone is set in the first-level gravity settling chamber, and the space inside the cyclone is a cyclone separation chamber. The cyclone is fixedly connected between the upper flower plate of the cyclone and the lower flower plate of the cyclone, and the central axis of the cyclone is perpendicular to the cyclone respectively. The upper flower plate of the cyclone and the lower flower plate of the cyclone, the dust-containing gas inlet of the cyclone is located in the first-level gravity settling chamber, and the separated gas outlet at the upper end of the cyclone and the dust discharge port at the lower end are connected with the second-level gravity settling chamber.

所述的旋风子上花板和旋风子下花板相互平行,旋风子上花板、旋风子下花板分别于与水平面呈30°夹角。 The upper flower plate of the cyclone and the lower flower plate of the cyclone are parallel to each other, and the upper flower plate of the cyclone and the lower flower plate of the cyclone are respectively at an angle of 30° with the horizontal plane.

所述的袋式收尘部分至少设有两个,每一个袋式收尘部分上均设有过滤进气口,重力旋风除尘部分上的旋风收尘出口分别于每一个袋式收尘部分上的过滤进气口相连通。 There are at least two bag-type dust-collecting parts, and each bag-type dust-collecting part is provided with a filter air inlet, and the cyclone dust-collecting outlet on the gravity cyclone dust-removing part is respectively connected to each bag-type dust-collecting part. connected to the filter air inlet.

本发明的有益效果是: The beneficial effects of the present invention are:

其一、本发明装置与高效重力旋风收尘与气箱式袋式收尘进行串联。使效旋风收尘与袋式收尘性能互补。本发明通过对重力旋风除尘部分进行改进,并将内部空间合理分割成重力沉降室和旋风分离室,有效对含尘气体多级处理,保证除尘效果,经重力旋风除尘部分处理后的气体经其出风口进入袋式除尘部分进行再次除尘,整个设备具有收尘效率高,运行费用小,占地面积小的优点。 One, the device of the present invention is connected in series with high-efficiency gravity cyclone dust collection and air box bag type dust collection. The effect of cyclone dust collection and bag dust collection are complementary. The present invention improves the gravity cyclone dedusting part and divides the internal space reasonably into a gravity settling chamber and a cyclone separation chamber to effectively treat the dusty gas in multiple stages to ensure the dust removal effect. The gas treated by the gravity cyclone dedusting part passes through its The air outlet enters the bag-type dust removal part for further dust removal. The whole equipment has the advantages of high dust collection efficiency, low operating cost and small footprint.

其二、在重力旋风除尘部分中,通过旋风子上花板、旋风子下花板和阻尼板阻隔成一级重力沉降室和二级重力沉降室,并将多个倾斜设置旋风子分布在一级重力沉降室内,所述一级重力沉降室由旋风子上花板、旋风子下花板和阻尼板包围而成,所述旋风子上花板、旋风子下花板分别与水平面呈锐角设置,阻尼板设置在远离进风口的一侧,并在所述阻尼板开设有重力沉降粉尘出口;通过以上结构改进,在一级重力沉降室内,气体流速降低,大颗粒物料在重力作用下,实现与气体的分离,同时,固体颗粒碰到旋风子外壁,失去惯性也得到分离,因此,分离效果更好;然后初步分离的气体进入旋风子内部再次将大颗粒粉尘分离掉,分离后的气体再次进入空间较大的二级重力沉降室,气体流速降低,大颗粒物料在重力作用下再次沿着倾斜的旋风子上花板落下收集,此结构达到最佳的分离效果;而且因为多个旋风子在密闭设置在一级重力沉降室内,所以系统保温效果非常好。 Second, in the dust removal part of the gravity cyclone, the first-level gravity settling chamber and the second-level gravity settling chamber are separated by the upper flower plate of the cyclone, the lower flower plate of the cyclone and the damping plate, and multiple inclined cyclones are distributed in the first-level In the gravity settling chamber, the first-level gravity settling chamber is surrounded by the upper flower plate of the cyclone, the lower flower plate of the cyclone and the damping plate, and the upper flower plate of the cyclone and the lower flower plate of the cyclone are respectively arranged at an acute angle with the horizontal plane, The damping plate is set on the side away from the air inlet, and a gravity settling dust outlet is opened on the damping plate; through the above structure improvement, in the first-level gravity settling chamber, the gas flow rate is reduced, and the large particle material is under the action of gravity. The separation of gas, at the same time, the solid particles hit the outer wall of the cyclone and are separated when they lose their inertia. Therefore, the separation effect is better; then the initially separated gas enters the interior of the cyclone to separate the large particles of dust again, and the separated gas enters again In the second-stage gravity settling chamber with a larger space, the gas flow rate is reduced, and the large particle materials fall and collect along the inclined cyclone upper flower plate again under the action of gravity. This structure achieves the best separation effect; and because multiple cyclones are in the The airtight setting is in the first-level gravity settling room, so the insulation effect of the system is very good.

其三、本发明将旋风子倾斜布置,将旋风子的中轴线分别垂直于旋风子上花板和旋风子下花板,同时将旋风子上花板、旋风子下花板的倾斜安装角度为30°,保证分离后粉尘顺利排出。 Its three, the present invention arranges the whirlwind obliquely, the central axis of the whirlwind is perpendicular to the whirlwind upper flower board and the whirlwind lower flower board respectively, and the oblique installation angle of the whirlwind upper flower board and the whirlwind lower flower board is 30° to ensure the smooth discharge of dust after separation.

其四、本发明装置上花板处于与水平倾斜安装,便于电收尘收下粉尘的排出。 Its four, the flower plate on the device of the present invention is installed at an inclination with the level, which is convenient for the discharge of the dust collected by the electric dust collector.

其五,该装置结构简单,便于检修,很容易清除内部的粉尘堆积现象,因此提高了设备的运转可靠性。 Fifth, the device has a simple structure, is convenient for maintenance, and is easy to remove internal dust accumulation, thereby improving the operational reliability of the equipment.

附图说明 Description of drawings

图1是本发明的主视图。 Fig. 1 is a front view of the present invention.

图2是本发明的俯视图。 Figure 2 is a top view of the present invention.

图3是本发明中重力旋风除尘部分的结构示意图。 Fig. 3 is a structural schematic diagram of the gravity cyclone dust removal part in the present invention.

图4是本发明中旋风子的结构示意图。 Fig. 4 is a schematic structural view of the cyclone in the present invention.

图中标记:1、壳体,101、进风口,102、洁净气体出口,103、出灰口,2、袋式除尘部分,201、滤袋,202、反吹装置,203、控制阀门,204、过滤进气口,3、重力旋风除尘部分, 301、重力沉降室,3011、一级重力沉降室,3012、二级重力沉降室,3013、旋风子上花板,3014、旋风子下花板,3015、阻尼板,3016、重力沉降粉尘出口,302、旋风子,3021、含尘气体进口,3022、分离气体出口,3023、排灰尘口,303、旋风收尘出口。 Marks in the figure: 1. shell, 101, air inlet, 102, clean gas outlet, 103, ash outlet, 2, bag dust removal part, 201, filter bag, 202, blowback device, 203, control valve, 204 , filter air inlet, 3, gravity cyclone dust removal part, 301, gravity settling chamber, 3011, first-level gravity settling chamber, 3012, second-level gravity settling chamber, 3013, cyclone upper flower plate, 3014, cyclone lower flower plate , 3015, damping plate, 3016, gravity sedimentation dust outlet, 302, cyclone, 3021, dusty gas inlet, 3022, separated gas outlet, 3023, dust discharge port, 303, cyclone dust collection outlet.

具体实施方式 Detailed ways

如图所示,一种集高效旋风收尘的气箱式袋式收尘器,包括带有进风口101、洁净气体出口102的壳体1,在壳体1的空腔内设有袋式收尘部分2和重力旋风除尘部分3,重力旋风除尘部分3和袋式收尘部分2串联连接,含尘气体通过进风口101进入壳体首先通过重力旋风除尘部分3处理,然后经过旋风收尘出口303排出后进入袋式收尘部分2处理后排出,在所述的重力旋风除尘部分3和袋式收尘部分2上均设有出灰口103,所述的重力旋风除尘部分3包括重力沉降室301和设置在重力沉降室内的旋风子302,所述的重力沉降室301由旋风子上花板3013、旋风子下花板3014和阻尼板3015将重力沉降室301内的空腔分割成一级重力沉降室3011和二级重力沉降室3012,进风口101与所述的一级重力沉降室3011相连通;所述一级重力沉降室3011由旋风子上花板3013、旋风子下花板3014和阻尼板3015包围而成,其中,旋风子上花板3013、旋风子下花板3014分别与水平面呈锐角设置,阻尼板3015设置在远离进风口101的一侧,并在所述阻尼板3015开设有重力沉降粉尘出口3016; As shown in the figure, an air box-type bag dust collector with high-efficiency cyclone dust collection includes a housing 1 with an air inlet 101 and a clean gas outlet 102, and a bag-type dust collector is provided in the cavity of the housing 1. The dust collection part 2 and the gravity cyclone dust removal part 3, the gravity cyclone dust removal part 3 and the bag type dust collection part 2 are connected in series, the dust-containing gas enters the housing through the air inlet 101 and is first processed by the gravity cyclone dust removal part 3, and then passed through the cyclone dust collection After the outlet 303 is discharged, it enters the bag type dust collection part 2 for treatment and then discharges. Both the gravity cyclone dust removal part 3 and the bag type dust collection part 2 are provided with an ash outlet 103. The gravity cyclone dust removal part 3 includes gravity The settling chamber 301 and the cyclone 302 arranged in the gravity settling chamber, the gravity settling chamber 301 is divided into a cavity in the gravity settling chamber 301 by the upper flower plate 3013 of the cyclone, the lower flower plate 3014 of the cyclone and the damping plate 3015. The first-level gravity settling chamber 3011 and the second-level gravity settling chamber 3012, the air inlet 101 communicates with the first-level gravity settling chamber 3011; 3014 and damping plate 3015, in which, the upper flower plate 3013 of the cyclone and the lower flower plate 3014 of the cyclone are respectively set at an acute angle with the horizontal plane, and the damping plate 3015 is set on the side away from the air inlet 101, and on the side of the damping plate 3015 is equipped with gravity sedimentation dust outlet 3016;

所述旋风子302设置在一级重力沉降室3011内,旋风子302内部的空间为旋风分离室,旋风子302固定连接在旋风子上花板3013和旋风子下花板3014之间,旋风子302的中轴线分别垂直于旋风子上花板3013和旋风子下花板3014,旋风子302的含尘气体进口3021位于一级重力沉降室3011内,旋风子302上端的分离气体出口3022和下端的排灰尘口3023均与二级重力沉降室3012相连通。 The cyclone 302 is set in the first-level gravity settling chamber 3011. The space inside the cyclone 302 is a cyclone separation chamber. The cyclone 302 is fixedly connected between the upper flower plate 3013 of the cyclone and the lower flower plate 3014 of the cyclone. The central axis of 302 is perpendicular to the upper flower plate 3013 of the cyclone and the lower flower plate 3014 of the cyclone respectively, the dust-containing gas inlet 3021 of the cyclone 302 is located in the first-level gravity settling chamber 3011, the separated gas outlet 3022 at the upper end of the cyclone 302 and the lower end The dust discharge ports 3023 of each are connected with the secondary gravity settling chamber 3012.

本发明中,所述的旋风子上花板3013和旋风子下花板3014相互平行,旋风子上花板3013、旋风子下花板3014分别于与水平面呈30°夹角。 In the present invention, the upper flower plate 3013 of the cyclone and the lower flower plate 3014 of the cyclone are parallel to each other, and the upper flower plate 3013 of the cyclone and the lower flower plate 3014 of the cyclone respectively form an included angle of 30° with the horizontal plane.

本发明,为了提高除尘效果,所述的袋式收尘部分2至少设有两个,每一个袋式收尘部分2上均设有过滤进气口204,重力旋风除尘部分3上的旋风收尘出口303分别于每一个袋式收尘部分2上的过滤进气口204相连通,旋风收尘出口303即为重力旋风除尘部分3处理后排出气体的端口,过滤进气口204即为袋式收尘部分2上的进气端口,通过设置多个袋式收尘部分2,保证收尘效率大大提高。 In the present invention, in order to improve the dust removal effect, at least two bag-type dust-collecting parts 2 are provided, and each bag-type dust-collecting part 2 is provided with a filter air inlet 204. The dust outlet 303 is respectively connected with the filter air inlet 204 on each bag type dust collection part 2, and the cyclone dust collection outlet 303 is the port for exhausting the gas after being processed by the gravity cyclone dust removal part 3, and the filter air inlet 204 is the bag filter. The air inlet port on the bag-type dust collection part 2 ensures that the dust collection efficiency is greatly improved by arranging a plurality of bag-type dust collection parts 2 .

本发明所述的袋式除尘部分2为现有成熟技术,可采用市售的袋式除尘器,本发明的主要改进点在于重力旋风除尘部分,因此关于袋式除尘部分并无过多描述,本文所述的袋式除尘部分是指气箱式袋式除尘设备,与脉冲式袋式除尘设备相类似,气箱式袋式除尘设备包括以下组件:对含尘气体进行过滤的滤袋201和用于清除滤袋外表沉积灰尘的反吹装置202,一般来说,含尘空气进入袋式除尘器后,通过滤袋过滤后排出,对应每一个滤袋箱的有个出气口,出气口有控制装置可以控制其开启,气箱上部与高压空气包相连,并通过一个控制阀门203控制。单个气箱内滤袋每工作一段时间,其气箱出气口关闭,高压气通过控制阀门使高压空气包与气箱上部联通,高压气体进入该气箱,对该气箱内滤袋进行反对,反吹气体从气箱下部进入另外气箱,滤袋外部的粉状物料落下并经壳体底部的出灰口排出收集。 The bag type dust removal part 2 described in the present invention is an existing mature technology, and a commercially available bag type dust remover can be used. The main improvement of the present invention lies in the gravity cyclone dust removal part, so there is not too much description about the bag type dust removal part. The bag type dust removal part mentioned in this article refers to the air box bag type dust removal equipment, which is similar to the pulse type bag type dust removal equipment. The air box type bag type dust removal equipment includes the following components: filter bag 201 for filtering dusty gas and The blowback device 202 used to remove the dust deposited on the surface of the filter bag. Generally speaking, after the dusty air enters the bag filter, it is filtered through the filter bag and then discharged. There is an air outlet corresponding to each filter bag box, and the air outlet has The control device can control its opening, and the upper part of the air box is connected with the high-pressure air bag, and is controlled by a control valve 203 . Every time the filter bag in a single air box works for a period of time, the air outlet of the air box is closed, and the high-pressure air passes through the control valve to connect the high-pressure air bag with the upper part of the air box, and the high-pressure gas enters the air box to oppose the filter bag in the air box. The blowback gas enters the other air box from the lower part of the air box, and the powdery material outside the filter bag falls and is discharged and collected through the ash outlet at the bottom of the shell.

本文所述的旋风子即为市场上所售的旋风分离器,本发明的创新点在整体的结构设计并结合倾斜设置的旋风分离器,而对于旋风分离器并无改进,常规的旋风分离器工作原理为:含粉尘气体受负压作用力沿旋风筒外壁切向进入,受离心力和重力双重作用力实现气体与固体的分离。 The cyclone described in this article is the cyclone separator sold on the market. The innovation of the present invention lies in the overall structural design combined with the cyclone separator which is arranged obliquely, but there is no improvement for the cyclone separator. The conventional cyclone separator The working principle is: the dust-containing gas enters tangentially along the outer wall of the cyclone under the force of negative pressure, and the separation of gas and solid is realized by the dual force of centrifugal force and gravity.

本装置中,将多个旋风子设置在一级重力沉降室内,根据处理风量,可以布置多个旋风子,所以处理风量可以满足工艺要求,同时因为多个旋风子在一个壳体内,所以系统保温效果好,且旋风子尺寸小,收尘效率高。 In this device, multiple cyclones are set in the first-level gravity settling chamber. According to the processing air volume, multiple cyclones can be arranged, so the processing air volume can meet the process requirements. At the same time, because multiple cyclones are in one shell, the system is insulated. The effect is good, and the size of the cyclone is small, and the dust collection efficiency is high.

Claims (1)

1. the air-box type bag filter collecting efficient cyclone and gather dust, comprise with air inlet (101), the housing (1) of clean gas outlet (102), bag type dust collection part (2) and gravity cyclone dust removal part (3) is provided with in the cavity of housing (1), gravity cyclone dust removal part (3) and bag type dust collection part (2) are connected in series, dusty gas is entered in housing also successively through gravity cyclone dust removal part (3) by air inlet (101), discharge after bag type dust collection part (2) process, described gravity cyclone dust removal part (3) and bag type dust collection part (2) are equipped with ash hole (103), it is characterized in that:
Described gravity cyclone dust removal part (3) comprises gravity settling chamber (301) and is arranged on the Whirlwind cyclone (302) of gravitational settling indoor, cavity in gravity settling chamber (301) is divided into one-level gravity settling chamber (3011) and secondary gravity settling chamber (3012) by Whirlwind cyclone upper face plate (3013), Whirlwind cyclone lower face plate (3014) and damping sheet (3015) by described gravity settling chamber (301), and air inlet (101) is connected with described one-level gravity settling chamber (3011); Described one-level gravity settling chamber (3011) is surrounded by Whirlwind cyclone upper face plate (3013), Whirlwind cyclone lower face plate (3014) and damping sheet (3015) and is formed, wherein, Whirlwind cyclone upper face plate (3013), Whirlwind cyclone lower face plate (3014) are arranged horizontal by acute angle respectively, damping sheet (3015) is arranged on the side away from air inlet (101), and offers gravitational settling dust outlet (3016) at described damping sheet (3015);
Described Whirlwind cyclone (302) is arranged in one-level gravity settling chamber (3011), the space of Whirlwind cyclone (302) inside is cyclone separating chamber, Whirlwind cyclone (302) is fixedly connected between Whirlwind cyclone upper face plate (3013) and Whirlwind cyclone lower face plate (3014), the axis of Whirlwind cyclone (302) is respectively perpendicular to Whirlwind cyclone upper face plate (3013) and Whirlwind cyclone lower face plate (3014), the dusty gas import (3021) of Whirlwind cyclone (302) is positioned at one-level gravity settling chamber (3011), the separated gas outlet (3022) of Whirlwind cyclone (302) upper end is all connected with secondary gravity settling chamber (3012) with the ash discharge dirt mouth (3023) of lower end,
Described Whirlwind cyclone upper face plate (3013) and Whirlwind cyclone lower face plate (3014) are parallel to each other, and Whirlwind cyclone upper face plate (3013), Whirlwind cyclone lower face plate (3014) are respectively at horizontal by 30 ° of angles;
Described bag type dust collection part (2) is at least provided with two, each bag type dust collection part (2) is equipped with filtered air inlet (204), and cyclone dust collection outlet (303) in gravity cyclone dust removal part (3) is connected respectively at the filtered air inlet (204) in each bag type dust collection part (2).
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CN108677846A (en) * 2018-06-25 2018-10-19 陕西通运专用汽车集团有限公司 Dry with demisting dust suppression function sweeps vehicle

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