CN202128991U - Vehicular bag-type dust collector for incineration vehicle - Google Patents
Vehicular bag-type dust collector for incineration vehicle Download PDFInfo
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- CN202128991U CN202128991U CN201120206834U CN201120206834U CN202128991U CN 202128991 U CN202128991 U CN 202128991U CN 201120206834 U CN201120206834 U CN 201120206834U CN 201120206834 U CN201120206834 U CN 201120206834U CN 202128991 U CN202128991 U CN 202128991U
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- 239000000428 dust Substances 0.000 title claims abstract description 31
- 238000013517 stratification Methods 0.000 claims 2
- 241000973497 Siphonognathus argyrophanes Species 0.000 claims 1
- 238000007599 discharging Methods 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 abstract description 14
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 229910052753 mercury Inorganic materials 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000009825 accumulation Methods 0.000 abstract description 4
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 3
- 231100001234 toxic pollutant Toxicity 0.000 abstract description 3
- 239000002253 acid Substances 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 abstract 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 21
- 239000003546 flue gas Substances 0.000 description 20
- 238000000746 purification Methods 0.000 description 6
- 239000002956 ash Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 229910052793 cadmium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 229910052804 chromium Inorganic materials 0.000 description 3
- 239000011651 chromium Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052745 lead Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- OGBQILNBLMPPDP-UHFFFAOYSA-N 2,3,4,7,8-Pentachlorodibenzofuran Chemical compound O1C2=C(Cl)C(Cl)=C(Cl)C=C2C2=C1C=C(Cl)C(Cl)=C2 OGBQILNBLMPPDP-UHFFFAOYSA-N 0.000 description 1
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000013256 coordination polymer Substances 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 150000002240 furans Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- FWMUJAIKEJWSSY-UHFFFAOYSA-N sulfur dichloride Chemical compound ClSCl FWMUJAIKEJWSSY-UHFFFAOYSA-N 0.000 description 1
- 230000007704 transition Effects 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
本实用新型涉及一种专用于移动式焚烧车的车载布袋除尘器。主要解决传统的布袋除尘器不适于焚烧车的技术问题。本实用新型的技术方案为:一种焚烧车车载布袋除尘器,为箱体结构,其特征是在箱体上部设有净室,在箱体下部设有积灰抽屉,箱体中间为尘室,在尘室中垂直方向间隔设有滤袋框架,滤袋框架外包覆滤袋,滤袋框架顶部固定在净室底部,在箱体下部的积灰抽屉上方设有进风口,在箱体上部的净室设有出风口。在箱体外设有气包,压缩空气经过滤器和两连件控制阀储存在气包内,气包底部通过管路接有放水阀。在滤袋框架顶部安置文氏管,文氏管与净室连通,文氏管管口设有控制管口开闭的电磁阀,气包通过管路接文氏管,脉冲控制仪接电磁阀。本实用新型主要用于焚烧车燃烧灰尘和有机剧毒污染物、酸性气态污染物、汞及重金属及其化合物的祛除。
The utility model relates to a vehicle-mounted bag filter specially used for a mobile incineration vehicle. It mainly solves the technical problem that the traditional bag filter is not suitable for incineration vehicles. The technical scheme of the utility model is: a bag-type dust collector on-board an incineration vehicle, which is a box structure, and is characterized in that a clean room is provided on the upper part of the box body, a dust accumulation drawer is provided on the lower part of the box body, and a dust chamber is in the middle of the box body , filter bag frames are arranged at vertical intervals in the dust room, and the filter bag frames are covered with filter bags. The upper clean room has an air outlet. There is an air bag outside the box, and the compressed air is stored in the air bag through a filter and two connecting control valves. The bottom of the air bag is connected with a water discharge valve through a pipeline. A Venturi tube is placed on the top of the filter bag frame, and the Venturi tube is connected with the clean room. The venturi tube nozzle is provided with a solenoid valve to control the opening and closing of the nozzle. The air bag is connected to the Venturi tube through the pipeline, and the pulse controller is connected to the solenoid valve. . The utility model is mainly used for removing combustion dust, organic highly toxic pollutants, acid gaseous pollutants, mercury, heavy metals and their compounds in incineration vehicles.
Description
技术领域 technical field
本实用新型涉及一种布袋除尘器,特别涉及一种专用于移动式焚烧车的车载布袋除尘器。 The utility model relates to a cloth bag dust collector, in particular to a vehicle-mounted cloth bag dust collector specially used for a mobile incineration vehicle.
背景技术 Background technique
布袋除尘器是一种高效的烟气净化装置,与静电除尘器、旋风除尘器、文立里除尘器、水幕除尘器等装置相比较,具有明显的优势,首先污染物质的除尘率最高,其次是不产生二次污染,三是价格适中。目前,被发达国家广泛应用,成为烟气净化系统中的关键装置。 The bag dust collector is an efficient flue gas purification device. Compared with electrostatic precipitators, cyclone dust collectors, Wenlili dust collectors, water curtain dust collectors and other devices, it has obvious advantages. First, the dust removal rate of pollutants is the highest. The second is that there is no secondary pollution, and the third is that the price is moderate. At present, it is widely used in developed countries and has become a key device in the flue gas purification system.
然而,布袋除尘器自发明应用以来的长时间内,都是应用于固定地点,从未应用于移动设备。其原因是体积较为庞大,需要占用较大的平面积和高度;而移动式设备的平面积受严格的局限,同时移动过程中的高度受到国家相关法规的严格限制。传统的布袋除尘器虽然在长期的应用过程中,先后有立式和卧式两种布袋除尘器问世。但都有一个共同之处,这就是体积较大,尤其是高度一般都在5m以上。这就决定了现有的高中型号的布袋除尘器都不可能用于焚烧车。 However, the bag filter has been used in fixed locations for a long time since its invention and application, and has never been used in mobile equipment. The reason is that the volume is relatively large, and it needs to occupy a large plane area and height; while the plane area of the mobile device is strictly limited, and the height during the movement is strictly limited by the relevant national regulations. Although the traditional bag filter has been used for a long time, two types of bag filter, vertical and horizontal, have come out. But they all have one thing in common, that is, the volume is relatively large, especially the height is generally above 5m. This determines that the existing high school models of bag filters cannot be used for incineration vehicles.
移动式焚烧车又必须采用烟气净化系统,而烟气净化系统中又不可缺少布袋除尘器。所以在确保布袋除尘器烟气处理量的前提下,必须开发一种体积小、高度低、烟气处理量大、污染物去除率高的全新结构布袋除尘器是非常必要的。从而使布袋除尘器的品种更多,用途更广。 The mobile incinerator must use a flue gas purification system, and the bag filter is indispensable in the flue gas purification system. Therefore, under the premise of ensuring the flue gas treatment capacity of the bag filter, it is very necessary to develop a new structure bag filter with small volume, low height, large flue gas treatment capacity and high pollutant removal rate. As a result, there are more varieties and wider uses of the bag filter.
发明内容 Contents of the invention
本实用新型的目的是提供一种专用于移动式焚烧车的车载布袋除尘器,主要解决传统的布袋除尘器不适于焚烧车的技术问题。 The purpose of this utility model is to provide a vehicle-mounted bag filter specially used for mobile incineration vehicles, mainly to solve the technical problem that the traditional bag filter is not suitable for incineration vehicles.
本实用新型的设计要求烟气处理量必须达到1200m3/min,而长度不可超过2.7m,宽不能超过2.2m,高不超过3m,烟气走向又必须是下进上出。除了原理不变外,其机构、壳体、支架、滤袋、积灰斗、脉冲高压高气清灰机构、净室等必须做全新的创新设计,同时还要具备抗震动、抗颠簸的性能,以适应焚烧在各种路况条件下的转场。 The design of the utility model requires that the flue gas treatment capacity must reach 1200m3/min, but the length cannot exceed 2.7m, the width cannot exceed 2.2m, and the height cannot exceed 3m. In addition to the same principle, its mechanism, shell, bracket, filter bag, dust hopper, pulse high-pressure high-air ash cleaning mechanism, clean room, etc. must have a new innovative design, and at the same time, it must have anti-vibration and anti-turbulence performance. Adapt to the transition of incineration under various road conditions.
本实用新型的技术方案为:一种焚烧车车载布袋除尘器,为箱体结构,其特征是在箱体上部设有净室,在箱体下部设有积灰抽屉,箱体中间为尘室,在尘室中垂直方向间隔设有滤袋框架,滤袋框架外包覆滤袋,滤袋框架顶部固定在净室底部,在箱体下部的积灰抽屉上方设有进风口,在箱体上部的净室设有出风口。在箱体外设有气包,压缩空气经过滤器和两连件控制阀储存在气包内,气包底部通过管路接有放水阀。在滤袋框架顶部安置文氏管,文氏管与净室连通,文氏管管口设有控制管口开闭的电磁阀,气包通过管路接文氏管,脉冲控制仪接电磁阀。 The technical scheme of the utility model is: a bag-type dust collector on-board an incineration vehicle, which is a box structure, and is characterized in that a clean room is provided on the upper part of the box body, a dust accumulation drawer is provided on the lower part of the box body, and a dust chamber is in the middle of the box body , filter bag frames are arranged at vertical intervals in the dust room, and the filter bag frames are covered with filter bags. The upper clean room has an air outlet. There is an air bag outside the box, and the compressed air is stored in the air bag through a filter and two connecting control valves. The bottom of the air bag is connected with a water discharge valve through a pipeline. A Venturi tube is placed on the top of the filter bag frame, and the Venturi tube is connected with the clean room. The venturi tube nozzle is provided with a solenoid valve to control the opening and closing of the nozzle. The air bag is connected to the Venturi tube through the pipeline, and the pulse controller is connected to the solenoid valve. .
本实用新型的有益技术效果是:通过在尘室内设置多个滤袋增加了处理面积,通过设置积灰抽屉可以方便的进行清灰,通过外设气包,可以使用高压气体对滤袋外表积灰进行清理。烟气中的颗粒物一部分是以无机灰分在热泳力的作用下存在于烟气中,而除汞以外的重金属及其化合物依附在颗粒物上存在于烟气中,汞以液态或气态的形式存在于烟气中并吸附于颗粒物上,二噁英类和呋喃类有机剧毒污染物同样依附于颗粒物存在于烟气中,本实用新型的作用不仅仅在于除尘,对于依附于颗粒灰尘上的绝大部分重金属及其化合物、有机剧毒污染物、液态或气态的汞也具有很好的祛除效果。 The beneficial technical effects of the utility model are: the processing area is increased by arranging a plurality of filter bags in the dust chamber, the ash can be cleaned conveniently by arranging the ash accumulation drawer, and the external area of the filter bag can be cleaned by high-pressure gas through the peripheral air bag. Ashes to clean up. Part of the particulate matter in the flue gas exists in the flue gas as inorganic ash under the action of thermophoretic force, while heavy metals and their compounds other than mercury are attached to the particulate matter and exist in the flue gas. Mercury exists in the form of liquid or gas. In the flue gas and adsorbed on the particles, dioxin and furan organic highly toxic pollutants are also attached to the particles and exist in the flue gas. The function of the utility model is not only for dust removal, but also for the vast Some heavy metals and their compounds, organic highly toxic pollutants, and liquid or gaseous mercury also have a good removal effect.
附图说明 Description of drawings
图1为本实用新型结构示意图。 Fig. 1 is the structural representation of the utility model.
图中:1-尘室,2-过滤器,3-两连件控制阀,4- 文氏管,5-滤袋框架,6-滤袋,7-净室,8-出风口,9-电磁阀,10-气包,11-放水阀,12-脉冲控制仪,13-进风口,14-积灰抽屉。 In the figure: 1-dust chamber, 2-filter, 3-two-piece control valve, 4-venturi tube, 5-filter bag frame, 6-filter bag, 7-clean room, 8-air outlet, 9- Solenoid valve, 10-air bag, 11-water discharge valve, 12-pulse controller, 13-air inlet, 14-dust drawer.
具体实施方式 Detailed ways
参照图1,一种焚烧车车载布袋除尘器,为箱体结构,在箱体上部设有净室7,在箱体下部设有积灰抽屉14,箱体中间为尘室1,在尘室中垂直方向间隔设有滤袋框架5,滤袋框架外包覆滤袋6,滤袋框架5顶部固定在净室底部,在箱体下部的积灰抽屉上方设有进风口13,在箱体上部的净室设有出风口8。在箱体外设有气包10,压缩空气经过滤器2和两连件控制阀3储存在气包10内,气包底部通过管路接有放水阀11。在滤袋框架顶部安置文氏管4,文氏管4与净室7连通,文氏管管口设有控制管口开闭的电磁阀9,气包10通过管路接文氏管4,脉冲控制仪12接电磁阀9。
Referring to Fig. 1, a kind of incineration vehicle-mounted bag filter has a box structure, and a
使用时,烟气冲冷却降温很合装置出来,从进风口13进入布袋除尘器内,流向各个尘室1,在引风机的强大抽力下烟气通过滤袋6,颗粒倍挡在滤袋外,一部分附着在滤袋外的滤料上,一部风在出室内烟气中飞扬进入滤袋内的去尘烟气通过文氏管4流向净室7,在引风机产生的(负压)抽力下从出口流出,通过引风机进烟囱将精华后的烟气排除。
When in use, the flue gas comes out of the cooling and cooling device, enters the bag filter from the
当布袋除尘器的工作阻力从正常值增大到一定量时,自动启动脉冲高压空气清除滤袋外的积灰,清除的积灰大部分跌落到积灰抽屉14中,一部分仍随烟气在热泳力和抽力的作用下存在于烟气中,净化效果见下表1。
When the working resistance of the bag filter increases from the normal value to a certain amount, the pulsed high-pressure air is automatically started to remove the dust outside the filter bag, and most of the removed dust falls into the
表1:本实用新型对烟气中污染物质的净化效果 Table 1: Purification effect of the utility model on pollutants in flue gas
注:酸性气态污染物(序号4 ~序号9),在进入布袋除尘器前就已经过两次中和去除;进入布袋除尘器后是对这几种物质的残量去除率。 Note: Acidic gaseous pollutants (No. 4 ~ No. 9) have been neutralized and removed twice before entering the bag filter; after entering the bag filter, it is the residual removal rate of these substances. the
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874251A (en) * | 2015-04-30 | 2015-09-02 | 浙江益森科技股份有限公司 | Vehicle-mounted dust collector |
| CN106268069A (en) * | 2015-06-01 | 2017-01-04 | 苏瑶炳 | A kind of dedusting air-supply arrangement for ceramic making |
| CN116459619A (en) * | 2023-02-27 | 2023-07-21 | 西安交通大学 | A flue gas water-saving collaborative multi-pollutant removal device and its working method |
-
2011
- 2011-06-20 CN CN201120206834U patent/CN202128991U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104874251A (en) * | 2015-04-30 | 2015-09-02 | 浙江益森科技股份有限公司 | Vehicle-mounted dust collector |
| CN106268069A (en) * | 2015-06-01 | 2017-01-04 | 苏瑶炳 | A kind of dedusting air-supply arrangement for ceramic making |
| CN116459619A (en) * | 2023-02-27 | 2023-07-21 | 西安交通大学 | A flue gas water-saving collaborative multi-pollutant removal device and its working method |
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