CN202844787U - Bag-type dust remover - Google Patents

Bag-type dust remover Download PDF

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Publication number
CN202844787U
CN202844787U CN201220334337.2U CN201220334337U CN202844787U CN 202844787 U CN202844787 U CN 202844787U CN 201220334337 U CN201220334337 U CN 201220334337U CN 202844787 U CN202844787 U CN 202844787U
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CN
China
Prior art keywords
dust
bag
air inlet
baffle plate
diameter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN201220334337.2U
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Chinese (zh)
Inventor
李志杰
邵光明
戴柏仙
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JIANGSU APOLLO AIR CONDITIONER PURIFICATION EQUIPMENT MANUFACTURING Co Ltd
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JIANGSU APOLLO AIR CONDITIONER PURIFICATION EQUIPMENT MANUFACTURING Co Ltd
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Priority to CN201220334337.2U priority Critical patent/CN202844787U/en
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Publication of CN202844787U publication Critical patent/CN202844787U/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

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  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The utility model discloses a bag-type dust remover. The bag-type dust remover comprises an access door, a net gas chamber and dust gas chambers, wherein a dust gas inlet is formed in the diameter of an air inlet of a lower box dust hopper part of the dust remover; a circular-arc shaped dust baffle plate is arranged above a position at which dust gas passes through the dust hopper; the dust baffle plate is as long as the air inlet of the dust remover; the circular-arc diameter of the dust baffle plate is equal to the diameter of the air inlet; and the height of the dust baffle plate is 1/3 of the diameter dimension of the air inlet. According to the bag-type dust remover provided by the utility model, the circular-arc dust baffle plate is designed at the dust gas inlet of the dust remover, so that large dust-containing particles are affected by gravity to drop into the dust hopper due to inertia and collision of the dust baffle plate when the dust-containing air enters the bag-type dust remover. Small dust particles enter a bag-type filter region, and are filtered by the bag-type dust remover. The filtering burden of the filter bag is greatly relieved; the dust removing efficiency is improved; and the change period and the service life of the filter bag are prolonged.

Description

布袋除尘器Bag filter

技术领域 technical field

本实用新型涉及到布袋除尘器。  The utility model relates to a bag filter. the

背景技术 Background technique

脉冲布袋除尘器是一种利用有机纤维或无机纤维布做成的过滤袋,将含尘气体中的粉尘经过滤而分离出来的一种高效除尘设备。除尘效率高,一般可达99%。袋式除尘器的主要元件是过滤布即滤袋,因工作环境的不同,滤袋需定期更换,才能保证设备的除尘效率。因此滤袋使用寿命的长短是除尘器设备除尘效率和整体寿命长短的关键。  The pulse bag filter is a kind of high-efficiency dust removal equipment that uses a filter bag made of organic fiber or inorganic fiber cloth to filter the dust in the dusty gas. The dust removal efficiency is high, generally up to 99%. The main component of the bag filter is the filter cloth or filter bag. Due to the different working environment, the filter bag needs to be replaced regularly to ensure the dust removal efficiency of the equipment. Therefore, the service life of the filter bag is the key to the dust removal efficiency and overall life of the dust collector. the

目前国内通风除尘上常用的脉冲除尘设备,传统做法是含尘气体从除尘器的尘气入口进入除尘器本体内部后直接进入与滤袋过滤区。  At present, the pulse dust removal equipment commonly used in domestic ventilation and dust removal, the traditional method is that the dust gas enters the dust collector body from the dust gas inlet of the dust collector and then directly enters the filter bag filter area. the

布袋除尘器属于中高效过滤器,捕集的粉尘粒径在0.5- 15μm之间,而一般除尘器入口的含尘,粒径分布在一个很大的范围之内,粉尘粒径大于20 μm粉尘直接进入布袋过滤区,会造成以下不良后果:1)除尘器工作一段时间后,靠近尘气入口的滤袋磨损程度远远大于其他位置滤袋的磨损程度;2)大颗粒粉尘直接进入布袋过滤区,加重了滤袋的过滤负担,降低了除尘效率,缩短了滤袋的更换周期和寿命。  The bag filter belongs to the medium and high efficiency filter, and the dust particle size captured is between 0.5-15 μm, while the dust at the entrance of the general dust collector has a particle size distribution within a large range, and the dust particle size is greater than 20 μm. Directly entering the bag filter area will cause the following adverse consequences: 1) After the dust collector has been working for a period of time, the wear degree of the filter bag near the dust gas inlet is far greater than that of other filter bags; 2) Large particles of dust directly enter the bag filter In this area, the filter burden of the filter bag is increased, the dust removal efficiency is reduced, and the replacement cycle and life of the filter bag are shortened. the

发明内容 Contents of the invention

本实用新型的目的就是要提供一种布袋除尘器,它能大大延长滤袋的更换周期和寿命。本实用新型的目的是这样实现的,布袋除尘器,包括检修门、净气室、尘气室,其特征在于:尘气入口位于除尘器设备的下箱体灰斗部分进风口直径处,在尘气经过处灰斗的上方设置有圆弧形挡灰板;所述的挡灰板长度与除尘器进风口长度相等,挡灰板圆弧直径与进风口直径相等,挡灰板的高度为进风口直径尺寸的1/3。本实用新型在除尘器尘气入口设计了一道圆弧形挡灰板,当含尘空气进入布袋除尘器,大的含尘颗粒由于惯性及与挡灰板的碰撞,受重力影响,而下沉,落入灰斗。含较小颗粒灰尘的空气进入布袋过滤 区,经布袋除尘过滤。大大减轻了滤袋的过滤负担,提高了除尘效率,延长了滤袋的更换周期和寿命。  The purpose of this utility model is to provide a bag filter, which can greatly extend the replacement cycle and life of the filter bag. The purpose of this utility model is achieved in this way. The bag dust collector includes an inspection door, a clean air chamber, and a dust air chamber. An arc-shaped ash baffle is arranged above the ash hopper where the dust gas passes; the length of the ash baffle is equal to the length of the air inlet of the dust collector, the diameter of the arc of the ash baffle is equal to the diameter of the air inlet, and the height of the ash baffle is 1/3 of the diameter of the air inlet. The utility model designs a circular arc-shaped ash baffle at the dust gas inlet of the dust collector. When the dusty air enters the bag filter, large dust particles will sink due to inertia and collision with the ash baffle. , into the ash hopper. The air containing smaller particles of dust enters the bag filter area and is filtered by the bag filter. It greatly reduces the filtering burden of the filter bag, improves the dust removal efficiency, and prolongs the replacement cycle and life of the filter bag. the

附图说明 Description of drawings

图1是本实用新型安装结构示意图;  Fig. 1 is a schematic diagram of the installation structure of the utility model;

图2是本实用新型结构示意图中的主视图;  Fig. 2 is the front view in the structural representation of the utility model;

图3是本实用新型结构示意图中的左视图;  Fig. 3 is the left view in the structural representation of the utility model;

1.引风口,2.净气出口,3.检修门,4.净气室,5.脉冲电磁,6.气包,7.尘气室,8.挡灰板,9.灰斗,10.卸灰阀,L为进风口长度,D为进风口直径。  1. Air inlet, 2. Clean air outlet, 3. Inspection door, 4. Clean air chamber, 5. Pulse electromagnetic, 6. Air bag, 7. Dust gas chamber, 8. Ash baffle, 9. Ash hopper, 10 .Ash unloading valve, L is the length of the air inlet, D is the diameter of the air inlet. the

具体实施方式 Detailed ways

下面结合附图对本实用新型作进一步说明;  Below in conjunction with accompanying drawing, the utility model is further described;

布袋除尘器,包括检修门3、净气室4、尘气室7,其特征在于:尘气入口位于除尘器设备下箱体灰斗9部分的进风口直径处,在尘气经过处灰斗的上方设置有圆弧形挡灰板;所述的挡灰板8长度与除尘器进风口长度相等,挡灰板8圆弧直径与进风口直径相等,挡灰板8的高度为进风口直径尺寸的1/3。具体实施时,如图所示,脉冲除尘器的尘气入口位于除尘器设备的下箱体灰斗部分进风口直径处,图中箭头方向表示箱体内的气流方向。在引风机的作用下,含尘气体从尘气入口进入,先经由挡灰板,大的含尘颗粒由于惯性及与挡灰板的碰撞,受重力影响,而下沉,直接落入灰斗;颗粒较小的灰尘则绕过挡灰板,经过滤袋的过滤,洁净的气体则穿过滤袋至滤袋内部被引风机带出箱体外,实现对含尘气体进行过滤的目的。  The bag dust collector includes an inspection door 3, a clean air chamber 4, and a dust chamber 7. It is characterized in that: the dust gas inlet is located at the diameter of the air inlet of the ash hopper 9 of the lower box of the dust collector equipment, and the ash hopper where the dust gas passes An arc-shaped gray baffle is arranged above; the length of the gray baffle 8 is equal to the length of the air inlet of the dust collector, the arc diameter of the ash baffle 8 is equal to the diameter of the air inlet, and the height of the ash baffle 8 is the diameter of the air inlet. 1/3 of the size. In specific implementation, as shown in the figure, the dust gas inlet of the pulse dust collector is located at the diameter of the air inlet of the dust hopper part of the lower box of the dust collector equipment, and the direction of the arrow in the figure indicates the airflow direction in the box. Under the action of the induced draft fan, the dust-laden gas enters from the dust gas inlet, and first passes through the ash baffle, and the large dust particles sink under the influence of gravity due to inertia and collision with the ash baffle, and fall directly into the ash hopper ;The dust with smaller particles bypasses the gray baffle and is filtered by the filter bag, and the clean gas passes through the filter bag to the inside of the filter bag and is taken out of the box by the induced draft fan to achieve the purpose of filtering the dusty gas. the

Claims (2)

1. sack cleaner, comprise access door (3), air-purifying chamber (4), dirt air chamber (7), it is characterized in that: dirt gas entrance is positioned at the air inlet diameter place of deduster equipment lower box ash bucket (9) part, is provided with circular arc dust block board (8) at dirt gas through the top of locating ash bucket (9).
2. sack cleaner according to claim 1, it is characterized in that: described dust block board (8) length and deduster air inlet equal in length, dust block board (8) arc diameter and air inlet equal diameters, the height of dust block board (8) is 1/3 of air inlet diameter dimension.
CN201220334337.2U 2012-07-11 2012-07-11 Bag-type dust remover Expired - Lifetime CN202844787U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201220334337.2U CN202844787U (en) 2012-07-11 2012-07-11 Bag-type dust remover

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201220334337.2U CN202844787U (en) 2012-07-11 2012-07-11 Bag-type dust remover

Publications (1)

Publication Number Publication Date
CN202844787U true CN202844787U (en) 2013-04-03

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201220334337.2U Expired - Lifetime CN202844787U (en) 2012-07-11 2012-07-11 Bag-type dust remover

Country Status (1)

Country Link
CN (1) CN202844787U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106975304A (en) * 2017-04-08 2017-07-25 安徽盛运重工机械有限责任公司 A kind of NEW TYPE OF COMPOSITE deduster
CN109124467A (en) * 2018-07-31 2019-01-04 芜湖通全科技有限公司 A kind of computer sound equipment Anti dust-escape device
CN113491910A (en) * 2021-07-26 2021-10-12 宁波众茂杭州湾热电有限公司 Boiler waste gas treatment device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106975304A (en) * 2017-04-08 2017-07-25 安徽盛运重工机械有限责任公司 A kind of NEW TYPE OF COMPOSITE deduster
CN109124467A (en) * 2018-07-31 2019-01-04 芜湖通全科技有限公司 A kind of computer sound equipment Anti dust-escape device
CN113491910A (en) * 2021-07-26 2021-10-12 宁波众茂杭州湾热电有限公司 Boiler waste gas treatment device

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CX01 Expiry of patent term

Granted publication date: 20130403

CX01 Expiry of patent term