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CN103239945A - A large-capacity double-pipe multi-group cyclone dust removal method - Google Patents

A large-capacity double-pipe multi-group cyclone dust removal method Download PDF

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Publication number
CN103239945A
CN103239945A CN2013101931078A CN201310193107A CN103239945A CN 103239945 A CN103239945 A CN 103239945A CN 2013101931078 A CN2013101931078 A CN 2013101931078A CN 201310193107 A CN201310193107 A CN 201310193107A CN 103239945 A CN103239945 A CN 103239945A
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dust removal
group
dust
cylinder
groups
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刘家富
何昕
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ZUNYI HONGXIN ENVIRONMENTAL PROTECTION TECHNOLOGYCO Ltd
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ZUNYI HONGXIN ENVIRONMENTAL PROTECTION TECHNOLOGYCO Ltd
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Abstract

一种大气量双管多组旋风式除尘方法,将两只单独的克雷资尔除尘器组成一组,共设2至6组,每组的进气分管均与主进气管以30度的角度连接组成并联式旋风净化除尘设备,每只管分别安装在除尘器的直筒体上部内,直筒体中心内为内筒体,内筒体顶端为净气出口,直筒体的下部连接有锥筒体,锥筒体内底部设有反射屏,底部设有灰斗,灰斗底部设有卸灰阀。本方案解决了大烟气量的除尘净化难题,克服了直径不能扩大,处理量又要大,对于粉尘粒度在20~40μm的除尘效率达98%,作为第一级除尘,它能延长风机使用寿命,延长后续袋式除尘器中的滤袋的寿命,降低了系统除尘器的运行成本。

A large-capacity double-pipe multi-group cyclone dust removal method. Two separate Krezier dust collectors are combined into one group, and there are 2 to 6 groups in total. The parallel cyclone purification and dust removal equipment is composed of angle connection. Each tube is installed in the upper part of the straight cylinder of the dust collector. The inner cylinder is in the center of the straight cylinder, and the top of the inner cylinder is the net gas outlet. The lower part of the straight cylinder is connected with a cone cylinder. , There is a reflective screen at the bottom of the cone, an ash hopper at the bottom, and an ash discharge valve at the bottom of the ash hopper. This solution solves the problem of dust removal and purification of large flue gas volume, overcomes the problem that the diameter cannot be expanded, and the processing capacity is large. The dust removal efficiency for dust particles with a particle size of 20-40 μm reaches 98%. As the first-stage dust removal, it can extend the use of fans. Life, prolong the life of the filter bag in the follow-up bag filter, and reduce the operating cost of the system dust collector.

Description

一种大气量双管多组旋风式除尘方法A large-capacity double-pipe multi-group cyclone dust removal method

技术领域 technical field

本发明涉及环保技术领域,尤其涉及大气量双管多组旋风除尘的方法。 The invention relates to the technical field of environmental protection, in particular to a large-capacity double-pipe multi-group cyclone dust removal method.

背景技术 Background technique

传统的旋风除尘是利用单只克雷资尔管对烟气量较小的硅铁炉、水泥厂以及其他的工业炉窑产生的烟气粉尘进行净化,对烟气中含粉尘粒径20~40μm的除尘率可达98%以上,但对于粉尘粒度<15μm以下的粉尘其效果较差,因此,将单只克雷资尔管旋风除尘用于第一级除法除化,将粉尘粒度大的首先除去。由于它的结构简单制造容易,造价低,处理能力大,因此,国内环保治理企业多家采用,但是它的致命卸陷是克雷资尔管的直径不能作得过大,只能在一定的直径范围内才能达到较好的除尘效果,如直径在220mm旋风管除尘器可处理54000m3/h烟气量,如再加大旋风管除尘器的直径除尘效率显著下降,为了解决大烟气量的除尘净化处理要求,又要使每台除尘效率达到最高峰值,经过多年的研究试验,在实践探索中终于找到了解决这一矛盾的办法。 The traditional cyclone dust removal is to use a single Kreiser tube to purify the flue gas dust produced by ferrosilicon furnaces, cement plants and other industrial furnaces with a small amount of flue gas, and the dust particle size in the flue gas is 20~ The dust removal rate of 40μm can reach more than 98%, but the effect is poor for dust with a particle size of less than 15μm. Remove first. Because of its simple structure, easy manufacture, low cost, and large processing capacity, it is adopted by many domestic environmental protection enterprises. Only within the diameter range can better dust removal effect be achieved. For example, a cyclone tube dust collector with a diameter of 220mm can handle a flue gas volume of 54000m 3 /h. If the diameter of the cyclone tube dust collector is increased, the dust removal efficiency will drop significantly. The requirements of dust removal and purification treatment must be met, and the dust removal efficiency of each unit must reach the highest peak. After years of research and testing, a solution to this contradiction has finally been found in practice and exploration.

发明内容 Contents of the invention

本发明的目的是针对现有技术的不足提供一种大气量双管多组旋风式除尘的方法,该 方法所采用的除尘设备为两只单独的旋风方向相反的克雷资尔旋风除尘器组合成一组,共有2~6组联合组成,每一组的含尘气体进气分管均与含尘气体主管以30~35°的角度相连接,组成一套联合式旋风净化除尘设备,作为第一级除尘设备,双管的组成包括两只同等大小的克雷资尔除尘器并联组合在一起为一组,每只克雷资尔管分别安装在除尘器的直筒体上部内,顶面环形密封,含尘气体从进气分管进入,中心为内筒体,内筒体顶端为净气出口,直筒体的下部连接有锥筒体,锥筒体内底部设有反射屏,含尘烟气从克雷资尔分管进入由直筒体内壁与内筒体外壁组成的圆环形旋风腔,依靠旋风气流的离心力,将粒度大的粉尘跌落在锥筒体内壁上下落,通过反射屏与锥筒体间的环形开口落入灰斗内,旋转的气流受到反射屏的阻挡,回转上升,通过净气出口进入下一工段的滤袋式除尘净化处理,锥筒体底部设有灰斗,灰斗底部设有卸灰阀。 The object of the present invention is to provide a method for large-capacity double-pipe multi-group cyclone dust removal in view of the deficiencies in the prior art. The dust removal equipment used in the method is a combination of two independent Krezier cyclone dust collectors with opposite cyclone directions. In one group, a total of 2 to 6 groups are combined. The dusty gas inlet pipe of each group is connected with the dusty gas main pipe at an angle of 30 to 35° to form a set of combined cyclone purification and dust removal equipment. As the first Class dust removal equipment, the composition of double pipes includes two Krezier dust collectors of the same size connected in parallel to form a group, each Krezier tube is installed in the upper part of the straight cylinder of the dust collector, and the top surface is annularly sealed , the dust-laden gas enters from the inlet branch pipe, the center is the inner cylinder, the top of the inner cylinder is the clean gas outlet, the lower part of the straight cylinder is connected to the cone cylinder, and the bottom of the cone cylinder is equipped with a reflection screen, and the dust-laden smoke flows from the g The Leizier tube enters the circular cyclone chamber composed of the inner wall of the straight cylinder and the outer wall of the inner cylinder, relying on the centrifugal force of the cyclone airflow, the dust with large particle size falls on the inner wall of the cone cylinder, and passes through the gap between the reflective screen and the cone cylinder. The circular opening of the ring falls into the ash hopper, the rotating air flow is blocked by the reflective screen, turns and rises, and enters the filter bag type dust removal and purification treatment in the next section through the net air outlet. There is a dust discharge valve.

采用本技术方案的有益效果:解决了在烟气量的除尘净化问题,也克服了克雷资尔管的直径不能扩大,处理量又要大,才能满足大烟气量的除尘净化设计要求,对于粉尘粒度在20~40μm的除尘效率可达98%,该设备作为第一级除尘净化处理,它能延长风机的使用寿命,延长后续的第二级袋式除尘器中的滤袋的寿命起了极其重要作用,从而降低了系统除尘器的运行成本。 The beneficial effect of adopting this technical solution: solves the problem of dust removal and purification in the amount of flue gas, and also overcomes that the diameter of the Kreiser tube cannot be expanded, and the processing capacity must be large to meet the design requirements for dust removal and purification of large flue gas volumes. The dust removal efficiency can reach 98% for the dust particle size of 20-40μm. This equipment is used as the first-stage dust removal and purification treatment, which can prolong the service life of the fan and extend the life of the filter bag in the subsequent second-stage bag filter. It plays an extremely important role, thereby reducing the operating cost of the system dust collector.

附图说明 Description of drawings

图1 为大气量双管多组旋风式除尘方法的并联组合结构示意图; Figure 1 is a schematic diagram of the parallel combined structure of the large-capacity double-pipe multi-group cyclone dust removal method;

图2 为图1中的一组剖面结构示意图; Fig. 2 is a group of cross-sectional structural schematic diagrams in Fig. 1;

图3 为一组克雷资尔旋风管投影示意图; Figure 3 is a schematic diagram of a group of Kreiser cyclone tube projections;

图中:1—净气出口,2—直筒体,3—内筒体,4—锥筒体,5—反射屏,6—灰斗,7—卸灰阀,8—进气分管,9—主进气管,10—主管与分管角度。 In the figure: 1—clean gas outlet, 2—straight cylinder, 3—inner cylinder, 4—cone cylinder, 5—reflecting screen, 6—ash hopper, 7—ash unloading valve, 8—intake pipe, 9— Main intake pipe, 10—director and branch pipe angle.

具体实施方式 Detailed ways

本发明所述的大气量双管多组旋风式除尘方法,具体实施方式分述如下:将两只单独的克雷资尔旋风除尘器组合成一组,共设2组、3组、4组、5组或6组联合组成,每一组的进气分管8均与主进气管9以30度的角度10相连接组成一套并联联合式旋风净化除尘设备作为第一级除尘,双管的组成包括两只同等大小克雷资尔管并联组合为一组,每只管分别安装在除尘器的直筒体2上部内,顶面环形封顶,含尘气体从主进气管9到进气分管8进入,直筒体2中心内为内筒体3,内筒体3顶端为净气出口1,直筒体2的下部连接有锥筒体4,锥筒体4内底部设有反射屏5,锥筒体4底部设有灰斗6,灰斗6底部设有卸灰阀7。 The large-scale double-pipe multi-group cyclone dust removal method described in the present invention is described in detail as follows: two separate Krezier cyclone dust collectors are combined into one group, and 2 groups, 3 groups, 4 groups, Composed of 5 groups or 6 groups, each group's intake pipe 8 is connected with the main intake pipe 9 at an angle of 30 degrees to form a set of parallel combined cyclone purification and dust removal equipment as the first stage of dust removal, the composition of double pipes It consists of two Kreiser tubes of the same size connected in parallel to form a group, each tube is installed in the upper part of the straight cylinder 2 of the dust collector, the top surface is ring-shaped, and the dust-laden gas enters from the main intake pipe 9 to the intake branch pipe 8, Inside the center of the straight cylinder 2 is the inner cylinder 3, the top of the inner cylinder 3 is the net gas outlet 1, the lower part of the straight cylinder 2 is connected with the cone cylinder 4, the inner bottom of the cone cylinder 4 is provided with a reflective screen 5, and the cone cylinder 4 An ash hopper 6 is arranged at the bottom, and an ash discharge valve 7 is arranged at the bottom of the ash hopper 6 .

经过该旋风除尘器的并联组合,使单一的克雷资尔管的旋风除尘达到最佳效果,彻底的解决了硅铁炉,水泥厂及各种工业炉窑的大气量烟尘除尘净化的难题,第一级除尘效果达98%,为后续进一步的滤袋式除尘创造了条件,延长了风机和滤袋的使用寿命,很受用户好评。  Through the parallel combination of the cyclone dust collector, the cyclone dust removal effect of a single Kreiser tube can be achieved, which completely solves the problem of dust removal and purification of large volume fume and dust in ferrosilicon furnaces, cement plants and various industrial furnaces. The first-stage dust removal effect reaches 98%, which creates conditions for further filter bag dust removal, prolongs the service life of fans and filter bags, and is well received by users. the

Claims (1)

1.一种大气量双管多组旋风式除尘方法,其特征在于:将两只单独的克雷资尔旋风除尘器组合成一组,共设2组、3组、4组、5组或6组联合组成,每一组的进气分管(8)均与主进气管(9)以30度的角度(10)相连接组成一套并联联合式旋风净化除尘设备作为第一级除尘,双管的组成包括两只同等大小克雷资尔管并联组合为一组,每只管分别安装在除尘器的直筒体(2)上部内,顶面环形封顶,含尘气体从主进气管(9)到进气分管(8)进入,直筒体(2)中心内为内筒体(3),内筒体(3)顶端为净气出口(1),直筒体(2)的下部连接有锥筒体(4),锥筒体(4)内底部设有反射屏(5),锥筒体(4)底部设有灰斗(6),灰斗(6)底部设有卸灰阀(7)。 1. A large-capacity double-pipe multi-group cyclone dust removal method is characterized in that: two independent Krezier cyclone dust collectors are combined into one group, and 2 groups, 3 groups, 4 groups, 5 groups or 6 groups are established. The air intake pipes (8) of each group are connected with the main air intake pipe (9) at an angle (10) of 30 degrees to form a set of parallel combined cyclone purification and dust removal equipment as the first stage dust removal, double pipes The composition includes two Kreiser tubes of the same size connected in parallel and combined into a group, each tube is respectively installed in the upper part of the straight cylinder (2) of the dust collector, the top surface is ring-shaped, and the dusty gas flows from the main intake pipe (9) to The air intake branch pipe (8) enters, the inner cylinder (3) is in the center of the straight cylinder (2), the top of the inner cylinder (3) is the net gas outlet (1), and the lower part of the straight cylinder (2) is connected with a cone cylinder (4), the inner bottom of the cone body (4) is provided with a reflective screen (5), the bottom of the cone body (4) is provided with an ash hopper (6), and the bottom of the ash hopper (6) is provided with an ash discharge valve (7).
CN2013101931078A 2013-05-23 2013-05-23 A large-capacity double-pipe multi-group cyclone dust removal method Pending CN103239945A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110871504A (en) * 2019-12-02 2020-03-10 安徽芜湖海螺建筑安装工程有限责任公司 Cutting and dust-collecting device for refractory bricks and cutting and dust-collecting method for refractory bricks

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2168373C1 (en) * 2000-06-21 2001-06-10 Волгоградский государственный технический университет Binary hydrocyclone
JP2004135700A (en) * 2002-10-15 2004-05-13 Toshiba Tec Corp Electric vacuum cleaner
EP1915940A1 (en) * 2005-08-19 2008-04-30 Suzhou Kingclean Floorcare Co., Ltd. A dust removing appliance of a parallel type cleaner
CN102600997A (en) * 2012-03-08 2012-07-25 无锡市华通电力设备有限公司 High-efficiency dust collection cyclone separator group

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2168373C1 (en) * 2000-06-21 2001-06-10 Волгоградский государственный технический университет Binary hydrocyclone
JP2004135700A (en) * 2002-10-15 2004-05-13 Toshiba Tec Corp Electric vacuum cleaner
EP1915940A1 (en) * 2005-08-19 2008-04-30 Suzhou Kingclean Floorcare Co., Ltd. A dust removing appliance of a parallel type cleaner
CN102600997A (en) * 2012-03-08 2012-07-25 无锡市华通电力设备有限公司 High-efficiency dust collection cyclone separator group

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
陈明绍等: "《除尘技术的基本理论与应用》", 31 December 1981, article "带有锥形内筒的旋风除尘器", pages: 456-459 *
陈明绍等: "《除尘技术的基本理论与应用》", 31 December 1981, 中国建筑工业出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110871504A (en) * 2019-12-02 2020-03-10 安徽芜湖海螺建筑安装工程有限责任公司 Cutting and dust-collecting device for refractory bricks and cutting and dust-collecting method for refractory bricks

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Application publication date: 20130814