CN201108786Y - bag collector - Google Patents
bag collector Download PDFInfo
- Publication number
- CN201108786Y CN201108786Y CNU2007203057717U CN200720305771U CN201108786Y CN 201108786 Y CN201108786 Y CN 201108786Y CN U2007203057717 U CNU2007203057717 U CN U2007203057717U CN 200720305771 U CN200720305771 U CN 200720305771U CN 201108786 Y CN201108786 Y CN 201108786Y
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- box
- filter
- bag
- collector
- filter box
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- 238000007599 discharging Methods 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 22
- 239000000463 material Substances 0.000 abstract description 14
- 238000004140 cleaning Methods 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 7
- 238000011084 recovery Methods 0.000 abstract description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 6
- 238000007664 blowing Methods 0.000 abstract description 6
- 239000003546 flue gas Substances 0.000 abstract description 6
- 238000012423 maintenance Methods 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 239000004566 building material Substances 0.000 abstract description 2
- -1 electric power Substances 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000005272 metallurgy Methods 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 description 14
- 238000000034 method Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000004071 soot 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
本实用新型属于环保除尘领域,特别是一种两级布袋过滤系统的袋式收集器,该袋式收集器包括:过滤箱体装置、灰斗(13)、进出风管(1,10)、脉冲清灰装置(3)、卸灰装置,其中所述过滤箱体装置由两级或以上过滤箱体串联组成,其中进风管(1)连接第一过滤箱体的下箱体,上箱体与相邻过滤箱体的下箱体连通,最终过滤箱体的上箱体与出风管(10)连接;各个上箱体中有由脉冲清灰装置(3)控制的喷吹管(8)。本实用新型设备重量轻,体积小,维修方便。该收集器物料回收率高,收集效果好,烟气排放浓度低,可广泛应用于冶金、建材、电力、化工、烟气除尘等行业的粉尘治理和物料回收。
The utility model belongs to the field of environmental protection and dust removal, in particular to a bag collector of a two-stage bag filter system. Pulse cleaning device (3), ash unloading device, wherein the filter box device is composed of two or more filter boxes connected in series, wherein the air inlet pipe (1) is connected to the lower box of the first filter box, and the upper box The body is connected with the lower box of the adjacent filter box, and the upper box of the final filter box is connected with the air outlet pipe (10); each upper box has a blowing pipe (8) controlled by a pulse cleaning device (3) ). The utility model equipment is light in weight, small in volume and convenient in maintenance. The collector has high material recovery rate, good collection effect and low flue gas emission concentration, and can be widely used in dust control and material recovery in metallurgy, building materials, electric power, chemical industry, flue gas dust removal and other industries.
Description
技术领域 technical field
本实用新型属于环保除尘领域,特别是一种两级布袋过滤系统的袋式收集器。The utility model belongs to the field of environmental protection and dust removal, in particular to a bag collector of a two-stage bag filter system.
背景技术 Background technique
除尘收集器主要由过滤箱体、灰斗、进出风管、过滤布袋、骨架、喷吹装置、卸灰装置等组成。含尘气体从进风管进入下箱体后,含尘气流通过滤袋进行过滤,阻留于滤袋外表面,净化后的气体进入上箱体,经排风管进入大气或净气管道,随着过滤工况地进行,滤袋上的粉尘层增厚,设备阻力增加,当设备阻力达到限定值时,由清灰控制装置按压差设定值或清灰时间设定值打开电控脉冲阀,喷吹气流经喷吹管对布袋进行喷吹,滤袋上的粉尘被抖落至灰斗中,由排灰装置排出。但是,现有技术的收集器一般都采用一级过滤系统的结构,即含有粉尘的烟尘从过滤箱体的下箱体进入进行净化,进入上箱体之后直接进入排风管;这样物料回收率不高、收集效果不理想。The dust collector is mainly composed of a filter box, an ash hopper, an air inlet and outlet, a filter bag, a skeleton, an injection device, and an ash unloading device. After the dust-laden gas enters the lower box from the air inlet pipe, the dust-laden air is filtered through the filter bag and retained on the outer surface of the filter bag. The purified gas enters the upper box, and enters the atmosphere or the clean air pipe through the exhaust pipe. As the filtering process progresses, the dust layer on the filter bag becomes thicker, and the resistance of the equipment increases. When the resistance of the equipment reaches the limit value, the dust removal control device turns on the electric control device according to the set value of the pressure difference or the set value of the dust removal time. With the pulse valve, the blowing air flows through the blowing pipe to spray the bag, and the dust on the filter bag is shaken off into the ash hopper and discharged by the ash discharge device. But the collector of prior art generally all adopts the structure of one-stage filtration system, promptly the soot that contains dust enters and purifies from the lower box body of filter box body, directly enters exhaust duct after entering upper box body; Not high, the collection effect is not ideal.
发明内容 Contents of the invention
本实用新型的目的是提供一种采用两级布袋过滤系统的特殊工艺结构的高效脉冲袋式收集器,可以提高物料回收率,收集效果好,降低烟气排放浓度。The purpose of this utility model is to provide a high-efficiency pulse bag collector with a special process structure using a two-stage bag filter system, which can improve material recovery rate, good collection effect, and reduce smoke emission concentration.
为了实现上述目的,本实用新型提供了如下技术方案:In order to achieve the above object, the utility model provides the following technical solutions:
一种袋式收集器,它包括过滤箱体装置,灰斗13,进出风管1、10,脉冲清灰装置3,卸灰装置,其中:A bag collector, which includes a filter box device, an
所述过滤箱体装置由两级或以上过滤箱体串联组成,其中进风管1连接第一过滤箱体的下箱体,上箱体与相邻过滤箱体的下箱体连通,最终过滤箱体的上箱体与出风管10连接;The filter box device is composed of two or more filter boxes connected in series, wherein the
各个上箱体中有由脉冲清灰装置3控制的喷吹管8。Each upper box has a
本实用新型的有益效果是:The beneficial effects of the utility model are:
与传统袋式除尘器、收尘器相比,新型高效脉冲袋式收集器采用两级布袋过滤系统的特殊工艺结构,具有以下技术特点:Compared with the traditional bag filter and dust collector, the new high-efficiency pulse bag collector adopts the special process structure of the two-stage bag filter system, and has the following technical characteristics:
1、物料回收率高、收集效果显著提高,极大地减少了物料的流失,对重要物料的回收再利用有着显著的经济效益。1. The material recovery rate is high, the collection effect is significantly improved, the loss of materials is greatly reduced, and the recovery and reuse of important materials has significant economic benefits.
2、由于采用两级过滤系统进行烟气处理,除尘效果好,烟气排放浓度低。2. Due to the use of a two-stage filter system for flue gas treatment, the dust removal effect is good and the flue gas emission concentration is low.
3、过滤风速低,滤袋使用寿命长。3. The filter wind speed is low, and the service life of the filter bag is long.
4、清灰效果好,操控方便快捷。4. The cleaning effect is good, and the operation is convenient and fast.
5、投资成本低,设备维护工作量少。5. Low investment cost and less equipment maintenance workload.
6、根据设备过滤面积及结构,可设置单灰斗或两个以上多个灰斗。6. According to the filtering area and structure of the equipment, a single ash hopper or more than two ash hoppers can be set.
附图简要说明Brief description of the drawings
图1为本实用新型袋式收集器第一实施例的结构示意图(单灰斗)。Fig. 1 is a schematic structural view of the first embodiment of the bag collector of the present invention (single ash hopper).
图2为本实用新型的第二实施例的结构示意图(两个灰斗)。Fig. 2 is a schematic structural view of the second embodiment of the present invention (two ash hoppers).
图3为本实用新型的第三实施例的结构示意图。Fig. 3 is a schematic structural diagram of a third embodiment of the present invention.
图4为图3中A向的侧示图。Fig. 4 is a side view of direction A in Fig. 3 .
附图2、3、4中各部件标记参见图1。Refer to Fig. 1 for the marks of each part in accompanying
具体实施方式 Detailed ways
1、组成部分:脉冲袋式物料收集器主要由过滤箱体、进出风管、布袋过滤系统、脉冲喷吹清灰系统、压缩气体管路及减压装置、检修装置、卸料装置等组成。1. Components: The pulse bag material collector is mainly composed of a filter box, an air inlet and outlet pipe, a bag filter system, a pulse jet dust cleaning system, a compressed gas pipeline, a decompression device, an overhaul device, and a discharge device.
2、过滤过程:含尘气体从袋式收集器的进风管道首先进入一级过滤系统(即1#箱体),含尘气流进入1#箱体通过滤袋进行过滤,大量粉尘或物料被截流于滤袋外表面上,透过滤袋的含尘气流达到一级净化后,通过1#箱体的上箱体进入2#箱体的下箱体,继而进入二级过滤系统,开始对气流进行二次净化过滤处理,经过两级过滤系统净化后的气流通过排风管道进入烟筒排入大气。2. Filtration process: The dust-laden gas enters the first-level filter system (namely, 1# box) from the air inlet pipe of the bag collector, and the dust-laden air enters the 1# box to be filtered through the filter bag, and a large amount of dust or materials are filtered. The flow is intercepted on the outer surface of the filter bag. After the dusty airflow passing through the filter bag reaches the first level of purification, it passes through the upper box of the 1# box and enters the lower box of the 2# box, and then enters the secondary filter system to start the airflow Perform secondary purification and filtration treatment, and the airflow purified by the two-stage filtration system enters the chimney through the exhaust duct and is discharged into the atmosphere.
3、清灰过程:随着过滤工况的进行,附着在滤袋上的粉尘层增厚,设备阻力增加,当设备阻力达到限定值时,由清灰控制装置按压差设定值或清灰时间设定值打开电磁脉冲阀,喷吹气流经过喷吹管对滤袋进行脉冲喷吹,滤袋上的粉尘被抖落至灰斗中,由此完成了对滤袋的一次清灰过程。集中在灰斗中的粉尘或物料定期通过收集器的卸灰装置转移至指定存储地点,实现物料的回收和再利用。3. Cleaning process: With the progress of the filtering condition, the dust layer attached to the filter bag becomes thicker, and the resistance of the equipment increases. The set value of graying time opens the electromagnetic pulse valve, and the blowing air flows through the blowing pipe to pulse blow the filter bag, and the dust on the filter bag is shaken off into the ash hopper, thus completing a cleaning process of the filter bag. The dust or materials concentrated in the ash hopper are regularly transferred to the designated storage place through the ash unloading device of the collector to realize the recycling and reuse of materials.
下面结合附图介绍本发明的具体实施例。Specific embodiments of the present invention will be described below in conjunction with the accompanying drawings.
实施例1Example 1
图1为本实施例的结构示意图(单灰斗),含尘气体通过进风管1进入1#下箱体2,透过滤袋12后经过第一次过滤,然后进入1#上箱体4、2#下箱体11,开始二次过滤,气流通过滤袋12过滤后进入2#上箱体9,然后经出风管10排出,过滤结束。经过过滤工况的不断进行,滤袋上的粉尘或物料越积越多,设备阻力增加,需进行清灰,脉冲清灰装置3启动,通过喷吹管8对滤袋进行脉冲喷吹清灰,被抖落的粉尘或物料落在灰斗13中,通过卸灰装置15运走。1#上箱体与2#上箱体间有隔板7相隔,上部均设顶部检修门6,上、下箱体之间有花格板相隔,整台设备由立柱14支撑。Fig. 1 is the structural diagram of this embodiment (single ash hopper), the dusty gas enters the 1#
实施例2Example 2
图2为本收集器的另一种实施例(两个灰斗)的结构形式。根据结构需要,可设置两个以上多个灰斗。其他结构与第一实施例相同。Fig. 2 is the structural form of another embodiment (two ash hoppers) of this collector. According to the structural requirements, more than two ash hoppers can be set. Other structures are the same as the first embodiment.
实施例3Example 3
如图3、4所示,某化工厂用脉冲袋式收集器,设备高度为10.636m,上下箱体总高度4.5m,宽度3.8m,过滤面积600m2,两级过滤工艺,过滤风速<1m/min。As shown in Figures 3 and 4, a chemical plant uses a pulse bag collector. The equipment height is 10.636m, the total height of the upper and lower boxes is 4.5m, the width is 3.8m, the filtration area is 600m 2 , two-stage filtration process, and the filtration wind speed is <1m. /min.
本实用新型采用两级布袋过滤系统,脉冲喷吹清灰装置进行清灰,设备重量轻,体积小,维修方便。该收集器物料回收率高,收集效果好,烟气排放浓度低,可广泛应用于冶金、建材、电力、化工、烟气除尘等行业的粉尘治理和物料回收。The utility model adopts a two-stage bag filter system and a pulse-jet dust-cleaning device to clean the dust. The equipment is light in weight, small in size and convenient in maintenance. The collector has high material recovery rate, good collection effect and low flue gas emission concentration, and can be widely used in dust control and material recovery in metallurgy, building materials, electric power, chemical industry, flue gas dust removal and other industries.
Claims (6)
Priority Applications (1)
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CNU2007203057717U CN201108786Y (en) | 2007-11-19 | 2007-11-19 | bag collector |
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CNU2007203057717U CN201108786Y (en) | 2007-11-19 | 2007-11-19 | bag collector |
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CN201108786Y true CN201108786Y (en) | 2008-09-03 |
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CNU2007203057717U Expired - Lifetime CN201108786Y (en) | 2007-11-19 | 2007-11-19 | bag collector |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106268136A (en) * | 2016-08-29 | 2017-01-04 | 合肥合意环保科技工程有限公司 | A kind of unit pulse bag-type dust-removing device |
CN106474836A (en) * | 2016-12-07 | 2017-03-08 | 威海航泰环保设备有限公司 | The gas cleaning of full-dry method Cremation Machine processes vertical sack cleaner |
CN109331587A (en) * | 2018-10-13 | 2019-02-15 | 广东嗨学云教育科技有限公司 | It is a kind of can intelligent blanking deduster |
-
2007
- 2007-11-19 CN CNU2007203057717U patent/CN201108786Y/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106268136A (en) * | 2016-08-29 | 2017-01-04 | 合肥合意环保科技工程有限公司 | A kind of unit pulse bag-type dust-removing device |
CN106474836A (en) * | 2016-12-07 | 2017-03-08 | 威海航泰环保设备有限公司 | The gas cleaning of full-dry method Cremation Machine processes vertical sack cleaner |
CN109331587A (en) * | 2018-10-13 | 2019-02-15 | 广东嗨学云教育科技有限公司 | It is a kind of can intelligent blanking deduster |
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C14 | Grant of patent or utility model | ||
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CP01 | Change in the name or title of a patent holder |
Address after: 100083 Beijing City, Haidian District Xueyuan Road District No. 30 Fangxing building room 702 Patentee after: Beijing bpbk energy-saving environmental protection Limited by Share Ltd Address before: 100083 Beijing City, Haidian District Xueyuan Road District No. 30 Fangxing building room 702 Patentee before: Beijing Bopeng Beike Technology Co., Ltd. |
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CX01 | Expiry of patent term |
Granted publication date: 20080903 |