CN207445851U - A kind of New Coal Mine efficient composite wet scrubber - Google Patents

A kind of New Coal Mine efficient composite wet scrubber Download PDF

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CN207445851U
CN207445851U CN201720884364.XU CN201720884364U CN207445851U CN 207445851 U CN207445851 U CN 207445851U CN 201720884364 U CN201720884364 U CN 201720884364U CN 207445851 U CN207445851 U CN 207445851U
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dust removal
dust
chamber
vibrating wire
filler
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张江石
刘金锋
王亚萌
杨雪松
张文越
许培辉
赵群
李晓曦
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China University of Mining and Technology Beijing CUMTB
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Abstract

本实用新型公开了一种新型煤矿高效复合式湿式除尘器,其特征在于:所述的除尘器是集水浴、填料、射流器、振弦珊于一体的高效复合式湿式除尘器,包含多级除尘,除尘过程从粗颗粒、细颗粒到微细颗粒依次净化:一级除尘用自激式水浴除尘部分对大颗粒粉尘进行捕集,二级除尘用填料除尘部分捕集较小颗粒粉尘,三级除尘用湿式振弦珊除尘部分捕集呼吸性粉尘;它处理风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点;它能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。

The utility model discloses a new high-efficiency composite wet dust collector for coal mines. Dust removal, the dust removal process is purified sequentially from coarse particles, fine particles to fine particles: the self-excited water bath dust removal part for the first-level dust removal collects large particle dust, the second-level dust removal uses the filler dust removal part to capture smaller particle dust, and the third-level dust removal Wet vibrating wire Shan dust removal part is used for dust removal to capture respirable dust; it has large air volume, high dust removal efficiency, is not easy to block, easy to clean, has the advantages of stable operation and convenient maintenance; it can effectively solve the problem of using a dust collector with a dust removal efficiency of up to However, the use of multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground, so as to deal with the problems of large dust generation and high concentration in the fully mechanized excavation working face of the coal mine.

Description

一种新型煤矿高效复合式湿式除尘器A New Coal Mine High Efficiency Composite Wet Dust Collector

技术领域technical field

本实用新型涉及煤矿除尘技术领域,特别是涉及一种新型煤矿高效复合式湿式除尘器。The utility model relates to the technical field of dust removal in coal mines, in particular to a novel high-efficiency composite wet dust collector for coal mines.

背景技术Background technique

综掘工作面是煤矿井下的最主要产尘点之一,随着煤矿采掘机械化程度的不断提高,高效、大功率掘进机的广泛使用,矿井开采强度越来越大,综掘工作面的粉尘产生量急剧增加,存在着粉尘产生量大、浓度高等问题,严重影响工人的身体健康,威胁矿井的安全生产。Fully mechanized excavation working face is one of the main dust-producing points in coal mines. With the continuous improvement of coal mining mechanization and the widespread use of high-efficiency and high-power roadheaders, the mine mining intensity is increasing, and the dust in fully mechanized excavation working face The production has increased sharply, and there are problems such as large dust production and high concentration, which seriously affect the health of workers and threaten the safe production of mines.

除尘器除尘是掘进工作面的高效防尘措施之一,目前国内外使用的除尘器,按照对粉尘颗粒捕集机制不同可分为四大类:机械式除尘器、过滤式除尘器、湿式除尘器、电除尘器。相比于其他除尘器,湿式除尘器具有除尘效率高,同时可以降温冷却、增加湿度和处理易燃、易爆及有害有毒气体的特点,目前已在冶金、矿山等行业中广泛应用。湿式除尘可以处理有害气体并且除尘效率较干式高,但相比干式除尘(例如袋式除尘器),单一除尘机理的湿式除尘器存在处理风量小、除尘效率低等问题,研制多机理综合型除尘器是提高除尘效率的发展方向。Dust removal by dust collector is one of the efficient dust prevention measures for tunneling face. At present, the dust collectors used at home and abroad can be divided into four categories according to the different dust particle collection mechanisms: mechanical dust collector, filter dust collector, wet dust collector device, electrostatic precipitator. Compared with other dust collectors, the wet dust collector has the characteristics of high dust removal efficiency, cooling, increasing humidity and handling flammable, explosive and harmful toxic gases. It has been widely used in metallurgy, mining and other industries. Wet dust collectors can handle harmful gases and have higher dust removal efficiency than dry dust collectors. However, compared with dry dust collectors (such as bag filters), wet dust collectors with a single dust removal mechanism have problems such as small air volume and low dust removal efficiency. Multi-mechanism comprehensive Type dust collector is the development direction to improve dust removal efficiency.

在实际应用中,除尘器也存在着容易堵塞、不便于清洗,运行不稳定,维修不方便等问题。有时为了达到所要求的除尘效率而将多个除尘设备串联使用,多级除尘系统有时有三级或四级除尘设备,但煤矿综掘工作面地质条件复杂、管路繁多、空间狭小,采用多级除尘系统时不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求。In practical applications, the dust collector also has problems such as easy blockage, inconvenient cleaning, unstable operation, and inconvenient maintenance. Sometimes in order to achieve the required dust removal efficiency, multiple dust removal equipments are used in series. The multi-stage dust removal system sometimes has three or four stages of dust removal equipment. The first-level dust removal system cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground.

实用新型内容Utility model content

针对上述情况,本实用新型的目的是提供一种新型煤矿高效复合式湿式除尘器,以解决上述现有技术存在的问题,这种除尘器在于它处理风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点;它能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。In view of the above situation, the purpose of this utility model is to provide a new type of high-efficiency composite wet dust collector for coal mines to solve the problems in the above-mentioned prior art. It has the advantages of stable operation and convenient maintenance; it can effectively solve the problem that the dust removal efficiency cannot be achieved by using a dust collector, and the multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground. In order to deal with the problems of large dust generation and high concentration in the fully mechanized excavation face of coal mines.

为实现上述目的,本实用新型提供了如下方案:In order to achieve the above object, the utility model provides the following scheme:

本实用新型提供一种新型煤矿高效复合式湿式除尘器,包括:第一供水管、进气室、进气口、除尘漏斗、调节手把、支撑件、第一排浆管、S型叶片、上叶片、下叶片、溢流水箱、溢流开口、第二排浆管、第二供水管、水位监测器、通气室、气雾室、填料室、填料下筛板、填料上筛板、填料球、第一喷嘴、射流室、射流器、文氏管、吸气室、喉管、扩散管、第二喷嘴、振弦栅、除尘水斗、除雾水斗、振弦栅管路、风机排水管,所述的除尘器是集水浴、填料、射流器、振弦珊于一体的高效复合式湿式除尘器,由自激式水浴除尘部分、填料除尘部分和湿式振弦栅除尘部分组成,其包含多级除尘,除尘过程从粗颗粒、细颗粒到微细颗粒依次净化:一级除尘用自激式水浴除尘部分对大颗粒粉尘进行捕集,二级除尘用填料除尘部分捕集较小颗粒粉尘,三级除尘用湿式振弦珊除尘部分捕集呼吸性粉尘。The utility model provides a new high-efficiency composite wet dust collector for coal mines, comprising: a first water supply pipe, an air inlet chamber, an air inlet, a dust removal funnel, an adjustment handle, a support member, a first slurry discharge pipe, S-shaped blades, Upper vane, lower vane, overflow water tank, overflow opening, second slurry discharge pipe, second water supply pipe, water level monitor, ventilation chamber, aerosol chamber, packing chamber, packing lower sieve plate, packing upper sieve plate, packing Ball, first nozzle, jet chamber, ejector, venturi tube, suction chamber, throat pipe, diffuser pipe, second nozzle, vibrating wire grid, dust removal bucket, mist removal bucket, vibrating wire grid pipeline, fan Drainage pipe, the dust collector is a high-efficiency composite wet dust collector integrating a water bath, filler, ejector, and vibrating wire. It is composed of a self-excited water bath dust removal part, a filler dust removal part and a wet vibrating wire grid dust removal part. It includes multi-stage dust removal, and the dust removal process is sequentially purified from coarse particles, fine particles to fine particles: the first-level dust removal uses a self-excited water bath dust removal part to capture large particles of dust, and the second-level dust removal uses a filler dust removal part to capture smaller particles Dust, three-stage dust removal uses wet vibrating wire Shan dust removal part to capture respirable dust.

优选的,所述自激式水浴除尘部分包括进气室、除尘漏斗、S型叶片、溢流水箱和气雾室,所述填料除尘部分包括填料室、填料层、填料上筛板、填料下筛板,所述湿式振弦栅除尘部分包括射流室、振弦栅和振弦栅管路,所述射流室包括气体进入腔和射流器;所述自激式水浴除尘部分、所述填料除尘部分和所述湿式振弦栅除尘部分由所述除尘器底部向上顺次连接。Preferably, the self-excited water bath dust removal part includes an air inlet chamber, a dust removal funnel, an S-shaped blade, an overflow water tank and an aerosol chamber, and the packing dust removal part includes a packing chamber, a packing layer, a packing upper sieve plate, and a packing lower screen plate, the wet vibrating wire grid dust removal part includes a jet chamber, a vibrating wire grid and a vibrating wire grid pipeline, the jet chamber includes a gas inlet chamber and a jet device; the self-excited water bath dust removal part, the packing dust removal part The dust removal part of the wet vibrating wire grid is sequentially connected upwards from the bottom of the dust collector.

优选的,所述进气室上开有与所述抽出式风筒连接的进气口,所述进气室和所述气雾室紧邻并排设置在所述除尘漏斗上方,且所述进气室和所述气雾室均与所述除尘漏斗连通;所述S型叶片水平布置于所述进气室和所述气雾室之间且位于所述除尘漏斗上方,所述S型叶片包括上叶片和下叶片,所述上叶片和所述下叶片之间形成净化室;所述除尘漏斗底部通过第一阀门连接有第一排浆管,所述除尘漏斗侧壁通过第二阀门连接有第一供水管。Preferably, the air inlet chamber is provided with an air inlet connected to the extraction type air duct, the air inlet chamber and the aerosol chamber are arranged side by side above the dust removal funnel, and the air inlet Both the chamber and the aerosol chamber communicate with the dust removal funnel; the S-shaped blades are horizontally arranged between the air inlet chamber and the aerosol chamber and above the dust removal funnel, and the S-shaped blades include The upper blade and the lower blade form a clean room between the upper blade and the lower blade; the bottom of the dust removal funnel is connected with a first slurry discharge pipe through a first valve, and the side wall of the dust removal funnel is connected with a The first water supply pipe.

优选的,所述除尘漏斗为可调式漏斗,所述进气室为可调进气室,所述除尘漏斗包括两端相互连接的锥体固定侧壁和锥体调整侧壁,所述进气室包括两端相互连接的柱体固定侧壁和柱体调整侧壁,所述锥体调整侧壁的上端与所述柱体调整侧壁的下端连接,所述锥体调整侧壁和所述柱体调整侧壁为可伸展侧壁,所述锥体调整侧壁通过支撑件连接有调节手把。Preferably, the dust removal funnel is an adjustable funnel, the air intake chamber is an adjustable air intake chamber, the dust removal funnel includes a cone fixed side wall and a cone adjustment side wall connected at both ends, the air intake The chamber includes a cylinder fixed side wall and a cylinder adjustment side wall connected at both ends, the upper end of the cone adjustment side wall is connected with the lower end of the cylinder adjustment side wall, the cone adjustment side wall and the cylinder adjustment side wall The cylinder adjustment side wall is an extendable side wall, and the cone adjustment side wall is connected with an adjustment handle through a support.

优选的,所述溢流水箱设置在所述除尘漏斗外侧并通过溢流开口与所述除尘漏斗连通,所述溢流水箱上部设有连通所述溢流水箱和所述气雾室的通气室,所述溢流水箱底部通过第三阀门连接有第二排浆管,所述溢流水箱侧壁通过第四阀门连接有第二供水管,所述溢流水箱内设有水位监测器Preferably, the overflow water tank is arranged on the outside of the dust removal funnel and communicates with the dust removal funnel through an overflow opening, and the upper part of the overflow water tank is provided with a ventilation chamber communicating with the overflow water tank and the aerosol chamber , the bottom of the overflow water tank is connected with the second slurry discharge pipe through the third valve, the side wall of the overflow water tank is connected with the second water supply pipe through the fourth valve, and the overflow water tank is provided with a water level monitor

优选的,所述填料室与所述气雾室连通,所述填料上筛板和所述填料下筛板分别设置在所述填料室的上下两端,所述填料层设置于所述填料上筛板和所述填料下筛板之间,所述填料上筛板上设置有第一喷嘴,所述第一喷嘴为高压喷雾喷嘴,所述第一喷嘴连接有第一自动喷雾系统。Preferably, the packing chamber communicates with the aerosol chamber, the packing upper sieve plate and the packing lower sieve plate are respectively arranged at the upper and lower ends of the packing chamber, and the packing layer is arranged on the packing Between the sieve plate and the lower sieve plate of the filler, a first nozzle is arranged on the upper sieve plate of the filler, the first nozzle is a high-pressure spray nozzle, and the first nozzle is connected with a first automatic spray system.

优选的,所述射流室包括气体进入腔和射流器,所述射流器包括文氏管和设置在所述文氏管内的第二喷嘴,所述文氏管包括依次连接且一体成型的吸气室、喉管和扩散管,所述气体进入腔一端与所述填料室的上端连接,所述气体进入腔的另一端与所述吸气室连接,所述扩散管与所述振弦栅管路连接,所述第二喷嘴连接有第二自动喷雾系统,所述振弦栅管路与所述扩散管连接的一端内设有多层所述振弦栅,前后相邻设置的所述振弦栅的振弦丝互相垂直。Preferably, the jet chamber includes a gas inlet chamber and an ejector, the ejector includes a venturi tube and a second nozzle arranged in the venturi tube, and the venturi tube includes sequentially connected and integrally formed suction One end of the gas inlet chamber is connected to the upper end of the packing chamber, the other end of the gas inlet chamber is connected to the suction chamber, and the diffusion pipe is connected to the vibrating wire grid tube The second nozzle is connected with the second automatic spraying system, the end of the vibrating wire grid pipeline connected with the diffuser pipe is provided with multiple layers of the vibrating wire grid, and the vibrating wire grids arranged adjacently before and after The vibrating wires of the string grid are perpendicular to each other.

优选的,沿风流流动方向,所述振弦栅管路在所述振弦栅的下方由前至后依次设置有除尘水斗和除雾水斗;所述振弦栅管路与抽出式风机的连接位置设置有风机排水管。Preferably, along the wind flow direction, the vibrating wire grid pipeline is provided with a dust removal water bucket and a demist water bucket in sequence from front to back under the vibration wire grid; The connection position of the fan is provided with a fan drain pipe.

本实用新型相对于现有技术取得了以下技术效果:Compared with the prior art, the utility model has achieved the following technical effects:

本实用新型提供的一种新型煤矿高效复合式湿式除尘器处理风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点,在大体不增加除尘系统所占空间大小的情况下除尘效率达到98.6%以上,能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。它的实施应用,对存在有害气体或可燃粉尘场所的空气净化技术也具有重要的意义,推广应用具有重大的社会效益和经济效益。The utility model provides a new high-efficiency composite wet dust collector for coal mines with large air volume, high dust removal efficiency, not easy to block, easy to clean, stable operation, convenient maintenance, etc., and generally does not increase the space occupied by the dust removal system. The lower dust removal efficiency reaches more than 98.6%, which can effectively solve the problem that the dust removal efficiency cannot be achieved by using a dust collector, and the multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground. There are problems such as large dust generation and high concentration in the fully mechanized excavation face of coal mines. Its implementation and application is also of great significance to the air purification technology in places with harmful gases or combustible dust, and its promotion and application has great social and economic benefits.

含尘风流由进气口进入除尘器,从进气室、S型叶片、气雾室、填料室、射流室、振弦栅、风机排水管经抽出式风机流出;除尘过程从粗颗粒、细颗粒到微细颗粒依次净化,包含多级除尘:一级除尘为自激式水浴除尘部分,用重力机理、惯性机理、离心机理对大颗粒粉尘进行捕集;二级除尘为填料除尘部分,用水浴机理、喷淋机理捕集较小颗粒粉尘;三级除尘为湿式振弦栅除尘部分,用振弦栅高效除尘机理捕集呼吸性粉尘。The dust-laden air flow enters the dust collector from the air inlet, and flows out from the air intake chamber, S-shaped blade, aerosol chamber, packing chamber, jet chamber, vibrating wire grid, and fan drain pipe through the withdrawable fan; the dust removal process starts from coarse particles, fine Particles to fine particles are purified sequentially, including multi-stage dust removal: the first stage dust removal is a self-excited water bath dust removal part, which uses gravity mechanism, inertia mechanism, and centrifugal mechanism to capture large particle dust; the second stage dust removal is a packing dust removal part, water bath Mechanism and spraying mechanism capture smaller particle dust; the three-stage dust removal is the dust removal part of the wet vibrating wire grid, and the high-efficiency dust removal mechanism of the vibrating wire grid is used to capture respirable dust.

附图说明Description of drawings

为了更清楚地说明本实用新型实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本实用新型的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the accompanying drawings required in the embodiments will be briefly introduced below. Obviously, the accompanying drawings in the following description are only the present invention. For some embodiments of the present invention, those of ordinary skill in the art can also obtain other drawings based on these drawings on the premise of not paying creative efforts.

图1是本实用新型一种新型煤矿高效复合式湿式除尘器的结构示意图;Fig. 1 is a structural schematic diagram of a novel coal mine high-efficiency composite wet dust collector of the utility model;

图2a是本实用新型一种新型煤矿高效复合式湿式除尘器的S型叶片上叶片的形状与尺寸(mm)示意图;Fig. 2 a is the shape and size (mm) schematic diagram of the blade on the S-shaped blade of a novel coal mine high-efficiency composite wet dust collector of the utility model;

图2b是本实用一种新型煤矿高效复合式湿式除尘器的S型叶片下叶片的形状与尺寸(mm)示意图;Fig. 2 b is a schematic diagram of the shape and size (mm) of the lower blade of the S-shaped blade of a novel coal mine high-efficiency composite wet dust collector of the present invention;

图2c是本实用新型一种新型煤矿高效复合式湿式除尘器的S型叶片组合示意图;Fig. 2c is a schematic diagram of the combination of S-shaped blades of a new coal mine high-efficiency composite wet dust collector of the utility model;

图3是本实用新型一种新型煤矿高效复合式湿式除尘器的射流器的结构示意图;Fig. 3 is a schematic structural view of a jet device of a novel coal mine high-efficiency composite wet dust collector of the utility model;

图4是本实用新型一种新型煤矿高效复合式湿式除尘器的振弦栅的结构示意图;Fig. 4 is a structural schematic diagram of a vibrating wire grid of a novel coal mine high-efficiency composite wet dust collector of the utility model;

图5是本实用新型一种新型煤矿高效复合式湿式除尘器的风机排水管结构示意图。Fig. 5 is a structural schematic diagram of a fan drain pipe of a new high-efficiency composite wet dust collector for coal mines according to the utility model.

图中:1-第一供水管;2-进气室;21-进气口;3-除尘漏斗;31-调节手把;32-支撑件;33- 第一排浆管;4-S型叶片;41-上叶片;42-下叶片;5-溢流水箱;51-溢流开口;52-第二排浆管;53-第二供水管;54-水位监测器;55-通气室;6-气雾室;7-填料室;71-填料下筛板;72-填料上筛板;73-填料球;74-第一喷嘴;8-射流室;9-射流器;91-文氏管;911-吸气室;912-喉管;913-扩散管;92-第二喷嘴;10-振弦栅;11-除尘水斗;12-除雾水斗;13-振弦栅管路;14-风机排水管;141-除尘器内圆筒,142- 风机外圆筒,143-风机排水管排水处;15-抽出式风机。In the figure: 1-the first water supply pipe; 2-intake chamber; 21-air inlet; 3-dust removal funnel; 31-adjusting handle; 32-support; Blade; 41-upper blade; 42-lower blade; 5-overflow tank; 51-overflow opening; 52-second slurry discharge pipe; 53-second water supply pipe; 54-water level monitor; 55-ventilation chamber; 6-Aerosol chamber; 7-Packing chamber; 71-Packing lower sieve plate; 72-Packing sieve plate; 73-Packing ball; 74-First nozzle; 8-Jet chamber; 9-Ejector; 91-Venturi Pipe; 911-suction chamber; 912-throat pipe; 913-diffusion pipe; 92-second nozzle; 10-vibrating wire grid; 11-dust bucket; 12-demist bucket; ; 14-fan drain pipe; 141-dust collector inner cylinder, 142-fan outer cylinder, 143-fan drain pipe drain; 15-drawing fan.

具体实施方式Detailed ways

下面将结合本实用新型实施例中的附图,对本实用新型实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of them. example. Based on the embodiments of the present utility model, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of the present utility model.

针对上述情况,本实用新型的目的是提供一种新型煤矿高效复合式湿式除尘器,以解决上述现有技术存在的问题,这种除尘器在于它处理风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点;它能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。In view of the above situation, the purpose of this utility model is to provide a new type of high-efficiency composite wet dust collector for coal mines to solve the problems in the above-mentioned prior art. It has the advantages of stable operation and convenient maintenance; it can effectively solve the problem that the dust removal efficiency cannot be achieved by using a dust collector, and the multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground. In order to deal with the problems of large dust generation and high concentration in the fully mechanized excavation face of coal mines.

为使本实用新型的上述目的、特征和优点能够更加明显易懂,下面结合附图和具体实施方式对本实用新型作进一步详细的说明。In order to make the above purpose, features and advantages of the utility model more obvious and understandable, the utility model will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.

本实用新型提供一种新型煤矿高效复合式湿式除尘器,如图1所示,包括:第一供水管1、进气室2、进气口21、除尘漏斗3、调节手把31、支撑件32、第一排浆管33、S型叶片4、上叶片41、下叶片42、溢流水箱5、溢流开口51、第二排浆管52、第二供水管53、水位监测器54、通气室55、气雾室6、填料室7、填料下筛板71、填料上筛板72、填料球73、第一喷嘴74、射流室8、射流器9、文氏管91、吸气室911、喉管912、扩散管913、第二喷嘴92、振弦栅10、除尘水斗11、除雾水斗13、振弦栅管路 13、风机排水管14、除尘器内圆筒141、风机外圆筒142、风机排水管排水处143,该除尘器是集水浴、填料、射流器、振弦珊于一体的高效复合式湿式除尘器,由自激式水浴除尘部分、填料除尘部分和湿式振弦栅除尘部分组成,其包含多级除尘,除尘过程从粗颗粒、细颗粒到微细颗粒依次净化:一级除尘用自激式水浴除尘部分对大颗粒粉尘进行捕集,二级除尘用填料除尘部分捕集较小颗粒粉尘,三级除尘用湿式振弦珊除尘部分捕集呼吸性粉尘。The utility model provides a new high-efficiency composite wet dust collector for coal mines, as shown in Figure 1, comprising: a first water supply pipe 1, an air inlet chamber 2, an air inlet 21, a dust removal funnel 3, an adjustment handle 31, and a support member 32. The first pulp pipe 33, the S-shaped blade 4, the upper blade 41, the lower blade 42, the overflow water tank 5, the overflow opening 51, the second pulp pipe 52, the second water supply pipe 53, the water level monitor 54, Vent chamber 55, aerosol chamber 6, packing chamber 7, filler lower sieve plate 71, filler upper sieve plate 72, filler ball 73, first nozzle 74, jet chamber 8, ejector 9, venturi tube 91, suction chamber 911, throat pipe 912, diffuser pipe 913, second nozzle 92, vibrating wire grid 10, dust removal water bucket 11, demisting water bucket 13, vibrating wire grid pipeline 13, fan drain pipe 14, dust collector inner cylinder 141, Fan outer cylinder 142, fan drain pipe drainage 143, the dust collector is a high-efficiency composite wet dust collector integrating water bath, filler, jet, and vibrating string. It is composed of self-excited water bath dust removal part, filler dust removal part and The wet-type vibrating wire grid dust removal part consists of multi-stage dust removal. The dust removal process is sequentially purified from coarse particles, fine particles to fine particles: the self-excited water bath dust removal part for the first-level dust removal collects large particles of dust, and the second-level dust removal is used The filler dust removal part captures smaller particle dust, and the third-stage dust removal uses a wet-type vibrating wire Shan dust removal part to capture respirable dust.

自激式水浴除尘部分包括进气室2、除尘漏斗3、S型叶片4、溢流水箱5和气雾室6,填料除尘部分包括填料室7、填料球73、填料上筛板72、填料下筛板71,湿式振弦栅除尘部分包括射流室8、振弦栅10和振弦栅管路13;自激式水浴除尘部分、填料除尘部分和湿式振弦栅除尘部分由除尘器底部向上顺次连接。The self-excited water bath dedusting part includes air inlet chamber 2, dust removal funnel 3, S-shaped blade 4, overflow water tank 5 and aerosol chamber 6, and the packing dedusting part includes packing chamber 7, packing ball 73, packing upper sieve plate 72, packing lower The sieve plate 71, the wet vibrating wire grid dust removal part includes the jet chamber 8, the vibrating wire grid 10 and the vibrating wire grid pipeline 13; connections.

采用上述结构,本实用新型提供的一种新型煤矿高效复合式湿式除尘器风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点,在大体不增加除尘系统所占空间大小的情况下除尘效率达到98.6%以上,能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。它的实施应用,对存在有害气体或可燃粉尘场所的空气净化技术也具有重要的意义,推广应用具有重大的社会效益和经济效益。With the above structure, the utility model provides a new high-efficiency composite wet dust collector for coal mines with large air volume, high dust removal efficiency, not easy to block, easy to clean, stable operation, convenient maintenance, etc., without increasing the space occupied by the dust removal system. The dust removal efficiency can reach more than 98.6% when the size is small, which can effectively solve the problem that the dust removal efficiency cannot be achieved by using a dust collector, and the multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground. , in order to deal with the problems of large dust generation and high concentration in the fully mechanized excavation face of coal mines. Its implementation and application is also of great significance to the air purification technology in places with harmful gases or combustible dust, and its promotion and application has great social and economic benefits.

含尘风流由进气口21进入除尘器,从进气室2、S型叶片4、气雾室6、填料室7、射流室8、振弦栅10、风机排水管14经抽出式风机15流出。The dust-laden wind enters the dust collector through the air inlet 21, and passes through the draw-out fan 15 from the air inlet chamber 2, S-shaped blade 4, aerosol chamber 6, packing chamber 7, jet chamber 8, vibrating wire grid 10, and fan drain pipe 14. flow out.

具体的方案中,自激式水浴除尘部分包括进气室2、除尘漏斗3、S型叶片4、溢流水箱5和气雾室6,进气室2上开有进气口21,进气室2和气雾室6并排设置在除尘漏斗3上方,且进气室2和气雾室6均与除尘漏斗3连通,S型叶片4水平安装布置于进气室2和气雾室6之间且位于除尘漏斗3上方, S型叶片4包括上叶片41和下叶片42,如图2a~2c所示,上叶片41和下叶片42之间形成净化室;除尘漏斗3底部通过第一阀门连接有第一排浆管33,除尘漏斗3侧壁通过第二阀门连接有第一供水管1,溢流水箱5设置在除尘漏斗3外侧并通过溢流开口51与除尘漏斗3连通,溢流水箱5上部设有连通溢流水箱5 和气雾室6的通气室55,溢流水箱5底部通过第三阀门连接有第二排浆管52,溢流水箱5侧壁通过第四阀门连接有第二供水管53,溢流水箱5内设有水位监测器54。In the specific scheme, the self-excited water bath dedusting part includes an air inlet chamber 2, a dust removal funnel 3, an S-shaped blade 4, an overflow water tank 5 and an aerosol chamber 6, and an air inlet 21 is opened on the air inlet chamber 2, and the air inlet chamber 2 and the aerosol chamber 6 are arranged side by side above the dust removal funnel 3, and both the air inlet chamber 2 and the aerosol chamber 6 communicate with the dust removal funnel 3, and the S-shaped blade 4 is installed horizontally between the air inlet chamber 2 and the aerosol chamber 6 and is located in the dust removal Above the funnel 3, the S-shaped vane 4 includes an upper vane 41 and a lower vane 42. As shown in Figures 2a to 2c, a clean room is formed between the upper vane 41 and the lower vane 42; the bottom of the dust removal funnel 3 is connected with a first The slurry discharge pipe 33 and the side wall of the dust removal funnel 3 are connected to the first water supply pipe 1 through the second valve. The overflow water tank 5 is arranged on the outside of the dust removal funnel 3 and communicates with the dust removal funnel 3 through the overflow opening 51. There is a ventilation chamber 55 connecting the overflow water tank 5 and the aerosol chamber 6, the bottom of the overflow water tank 5 is connected with the second slurry discharge pipe 52 through the third valve, and the side wall of the overflow water tank 5 is connected with the second water supply pipe 53 through the fourth valve , The overflow water tank 5 is provided with a water level monitor 54.

在进一步的方案中,除尘漏斗3为可调式漏斗,进气室2为可调式进气室,除尘漏斗3包括两端相互连接的锥体固定侧壁和锥体调整侧壁,进气室包括两端相互连接的柱体固定侧壁和柱体调整侧壁,锥体调整侧壁的上端与柱体调整侧壁的下端连接,锥体调整侧壁和柱体调整侧壁为可伸展侧壁,锥体调整侧壁通过支撑件连接有调节手把。In a further solution, the dust removal funnel 3 is an adjustable funnel, the air intake chamber 2 is an adjustable air intake chamber, the dust removal funnel 3 includes a cone fixed side wall and a cone adjustment side wall connected to each other at both ends, and the air intake chamber includes The fixed side wall of the cylinder and the adjustment side wall of the cylinder connected at both ends, the upper end of the adjustment side wall of the cone is connected with the lower end of the adjustment side wall of the cylinder, and the adjustment side wall of the cone and the adjustment side wall of the cylinder are stretchable side walls , the cone adjustment side wall is connected with an adjustment handle through a support piece.

可伸展侧壁可以为弹性可伸展侧壁;也可以为非弹性可伸展侧壁,例如可伸展侧壁的一端与固定侧壁的一端固定连接,可伸展侧壁的另一端可相对于固定侧壁的另一端移动并能够形成密封,即能够实现可伸展侧壁的伸展。通过移动调节手把31,可以带动可伸展侧壁发生弹性变形或周向移动,从而能够调节进气室2和除尘漏斗3断面面积,从而使同一工作面时,进气口21气体流速可调节;本实用新型提供的一种新型煤矿高效复合式湿式除尘器应用于不同的工作面时,可调节可伸展侧壁,从而实现灵活调节进气室2和除尘漏斗3的断面面积以调节其内部的通气量,达到除尘净化的最佳速度。The stretchable sidewall can be an elastic stretchable sidewall; it can also be a non-elastic stretchable sidewall, for example, one end of the stretchable sidewall is fixedly connected with one end of the fixed sidewall, and the other end of the stretchable sidewall can be opposite to the fixed sidewall. The other end of the wall moves and enables a seal, ie, enables expansion of the extensible side wall. By moving the adjusting handle 31, the stretchable side wall can be driven to elastically deform or move in the circumferential direction, so that the cross-sectional area of the air inlet chamber 2 and the dust removal funnel 3 can be adjusted, so that the gas flow rate of the air inlet 21 can be adjusted on the same working surface When the utility model provides a new high-efficiency composite wet dust collector for coal mines, when it is applied to different working faces, the side wall can be adjusted and stretched, so as to realize the flexible adjustment of the cross-sectional area of the air inlet chamber 2 and the dust removal funnel 3 to adjust its interior The ventilation volume reaches the best speed of dust removal and purification.

在进一步的方案中,除尘漏斗3底部通过第一阀门连接有第一排浆管33,除尘漏斗3侧壁通过第二阀门连接有第一供水管1,溢流水箱5设置在除尘漏斗3外侧并通过溢流开口51与除尘漏斗3连通,溢流水箱5上部设有连通溢流水箱5和气雾室6的通气室55,溢流水箱5底部通过第三阀门连接有第二排浆管52,溢流水箱5侧壁通过第四阀门连接有第二供水管53,溢流水箱5内设有水位监测器54。In a further solution, the bottom of the dust removal funnel 3 is connected to the first slurry discharge pipe 33 through the first valve, the side wall of the dust removal funnel 3 is connected to the first water supply pipe 1 through the second valve, and the overflow water tank 5 is arranged outside the dust removal funnel 3 And communicate with the dust removal funnel 3 through the overflow opening 51, the upper part of the overflow water tank 5 is provided with a ventilation chamber 55 connecting the overflow water tank 5 and the aerosol chamber 6, and the bottom of the overflow water tank 5 is connected with the second slurry discharge pipe 52 through the third valve A second water supply pipe 53 is connected to the side wall of the overflow water tank 5 through a fourth valve, and a water level monitor 54 is arranged in the overflow water tank 5 .

溢流水箱5用来控制除尘漏斗3内的水位及水位的稳定性,在溢流水箱5上设置通气室55使溢流水箱5与气雾室55压力相等,溢流开口51设在除尘漏斗3里,用溢流开口51代替易堵塞的溢流管将除尘漏斗3中的水与溢流水箱5连通起来,通过溢流水箱5反映出除尘漏斗3内的水面高度,若水位监测器54监测到溢流水箱5内的水位较低时,控制系统通过第二供水管53向溢流水箱5内供水以保证除尘器的水位恒定,从而保证除尘效率的稳定。The overflow water tank 5 is used to control the water level and the stability of the water level in the dust removal funnel 3. A ventilation chamber 55 is set on the overflow water tank 5 to make the pressure of the overflow water tank 5 and the aerosol chamber 55 equal, and the overflow opening 51 is located in the dust removal funnel 3 mile, replace the overflow pipe that is easy to block with overflow opening 51 and connect the water in the dust removal funnel 3 with the overflow water tank 5, reflect the water surface height in the dust removal funnel 3 by the overflow water tank 5, if the water level monitor 54 When it is detected that the water level in the overflow water tank 5 is low, the control system supplies water to the overflow water tank 5 through the second water supply pipe 53 to ensure that the water level of the dust collector is constant, thereby ensuring the stability of the dust removal efficiency.

更具体的方案中,进气室2是半径为0.28m(其具体尺寸需根据应用地点的实际情况确定)的圆柱腔体,为使进入除尘器内的气体均匀分布于整个S型叶片4,进气口21应高出S型叶片4一定高度,例如0.5m;为防止除尘漏斗3堵塞,应确保除尘漏斗3的角度适当大些,可调式漏斗初始漏斗角度设为 55°,纵深0.6m。In a more specific solution, the air inlet chamber 2 is a cylindrical cavity with a radius of 0.28m (the specific size needs to be determined according to the actual situation of the application site). In order to make the gas entering the dust collector evenly distributed throughout the S-shaped blade 4, The air inlet 21 should be higher than the S-shaped blade 4 by a certain height, such as 0.5m; in order to prevent the dust removal funnel 3 from clogging, the angle of the dust removal funnel 3 should be ensured to be appropriately larger, and the initial funnel angle of the adjustable funnel is set to 55°, and the depth is 0.6m .

上叶片41和下叶片42间的净化室中气流速度可到达18~30m/s,进气速度一般不超过18m/s。为避免腐蚀和便于清灰,S型叶片4材质使用不锈钢,S型叶片4的形状及尺寸如2a所示,S型叶片4安装时必须水平,组装后的叶片组合如图2b所示。The air velocity in the clean room between the upper blade 41 and the lower blade 42 can reach 18~30m/s, and the intake velocity is generally no more than 18m/s. In order to avoid corrosion and facilitate dust removal, the S-shaped blade 4 is made of stainless steel. The shape and size of the S-shaped blade 4 are shown in 2a. The S-shaped blade 4 must be installed horizontally. The assembled blade combination is shown in Figure 2b.

溢流开口51开孔设计为100mm×50mm左右,溢流水箱5的控制水位为20mm,即溢流堰高出上叶片41下沿20mm,水位波动不超过5mm,为减少水面波动,第一供水管1、第二供水管53和溢流开口51 均埋设在控制水位以下。The overflow opening 51 is designed to be about 100mm × 50mm, and the control water level of the overflow water tank 5 is 20mm, that is, the overflow weir is 20mm higher than the lower edge of the upper blade 41, and the fluctuation of the water level is not more than 5mm. In order to reduce the fluctuation of the water surface, the first water supply The pipe 1, the second water supply pipe 53 and the overflow opening 51 are all buried below the control water level.

采用上述结构,当除尘器通电后,除尘器通过第一供水管1冲水至启动水位,水位高度与上叶片41下沿平齐,然后启动抽出式风机15。含尘气体由进气口21流入至进气室2,由于气体流动断面扩大,气体流速变慢,大颗粒粉尘重力沉降,气流转弯向下冲击液面,激起大量水滴进入S型叶片4,水气充分混合,细小尘粒被捕集。气流从风道流出S型叶片4后进入气雾室6,气体流动断面再次扩大,速度突然降低,含水滴的粉尘掉落水中被水捕集,气体继续向上流动,沉至除尘漏斗3底部,而被水捕集的尘粒沉至除尘漏斗3底部,通过第一排浆管33定期排出。With the above structure, when the dust collector is energized, the dust collector is flushed to the starting water level through the first water supply pipe 1, and the water level is flush with the lower edge of the upper blade 41, and then the draw-out fan 15 is started. The dust-laden gas flows into the air inlet chamber 2 from the air inlet 21. Due to the expansion of the gas flow section, the gas flow velocity slows down, and the large particles of dust settle down by gravity. The water and air are fully mixed, and the fine dust particles are captured. The air flow flows out of the S-shaped blade 4 from the air duct and enters the aerosol chamber 6. The gas flow section expands again, and the speed suddenly decreases. The dust containing water drops falls into the water and is captured by the water. The dust particles collected by water sink to the bottom of the dust removal funnel 3 and are regularly discharged through the first row of slurry pipes 33 .

气雾室6不必设置挡水板,减少了气雾室6的压力损失。气雾室6横截面尺寸主要取决于填料室7,通过实验确定可以使填料室7中填料上下翻滚并取得最佳除尘效率时的风流速度,由此计算出断面面积;气雾室6断面面积应适当大些,可以使含尘气流中的粘有大水滴的尘粒由于速度忽然减小(流动断面增大)有足够的时间靠自重作用沉降至水中。The aerosol chamber 6 does not need to be provided with a water baffle, which reduces the pressure loss of the aerosol chamber 6 . The cross-sectional size of the aerosol chamber 6 mainly depends on the packing chamber 7. The air flow velocity at which the packing in the packing chamber 7 can roll up and down and obtain the best dust removal efficiency is determined through experiments, and the cross-sectional area is calculated from this; the cross-sectional area of the aerosol chamber 6 It should be appropriately larger, so that the dust particles with large water droplets in the dust-laden airflow have enough time to settle into the water by their own weight due to the sudden decrease in velocity (the flow section increases).

在另一种具体的方案中,填料除尘部分包括填料室7、填料球73、填料上筛板72、填料下筛板71,填料室7与气雾室6连通,填料上筛板72和填料下筛板71分别设置在填料室7的上下两端,填料放置于填料上筛板72和填料下筛板71之间,填料上筛板72上设置有第一喷嘴74。In another specific scheme, the filler dust removal part includes a filler chamber 7, a filler ball 73, an upper sieve plate 72 for the filler, and a lower sieve plate 71 for the filler, the filler chamber 7 communicates with the aerosol chamber 6, and the upper sieve plate 72 and the filler The lower sieve plate 71 is respectively arranged at the upper and lower ends of the packing chamber 7, and the packing is placed between the upper packing sieve plate 72 and the lower packing sieve plate 71, and the upper packing sieve plate 72 is provided with a first nozzle 74.

更具体的方案中,填料室7筒体直径不小于0.38m,填料层选用非固定填料层,填料层的填料为直径38mm的聚丙烯材料制成的形状类似QTL-150T的填料球73。填料球堆放4层,堆放高度152mm,填料下筛板71和填料上筛板72筛板间距456mm,填料下筛板71和填料上筛板72的珊条间的尺寸都是20mm,填料上筛板72采用尼龙丝制成的珊条拦截填料球73,填料下筛板71采用合金钢丝制成的珊条支撑填料球 73。第一喷嘴74为高压喷雾喷嘴,使填料球73可以充分浸润,第一喷嘴74连接有第一自动喷雾系统。In a more specific solution, the diameter of the packing chamber 7 is not less than 0.38m, the packing layer is a non-fixed packing layer, and the packing layer is a packing ball 73 made of polypropylene material with a diameter of 38mm and similar in shape to QTL-150T. Packing balls are stacked in 4 layers with a stacking height of 152mm. The distance between the lower sieve plate 71 and the upper sieve plate 72 is 456mm. Plate 72 adopts the slats made of nylon wire to intercept packing ball 73, and the sieve plate 71 adopts the slats made of alloy steel wire to support packing ball 73 under the filler. The first nozzle 74 is a high-pressure spray nozzle, so that the filler ball 73 can be fully soaked, and the first nozzle 74 is connected with a first automatic spray system.

采用上述结构,填料除尘部分利用第一喷嘴74向填料喷淋带有添加剂的喷淋液以及填料的惯性碰撞、拦截、吸附作用,一方面填料球73在气流的作用下上下翻滚、相互冲刷,可增加粉尘与喷淋液的接触时间,另一方面,喷淋液润湿填料,在填料球73表明形成气液界面传质,增加捕尘效果。被捕集的粉尘还能通过填料球73的相互碰撞和喷淋液的冲刷落入除尘漏斗,填料球73的相互碰撞还能起到清洗填料球73的目的,从而使含尘气体与溶液充分接触完成除尘过程。With the above structure, the filler dust removal part uses the first nozzle 74 to spray the spray liquid with additives to the filler and the inertial collision, interception and adsorption of the filler. On the one hand, the filler balls 73 roll up and down under the action of the air flow and wash each other The contact time between the dust and the spray liquid can be increased. On the other hand, the spray liquid wets the filler and forms a gas-liquid interface mass transfer in the filler ball 73, increasing the dust collection effect. The collected dust can also fall into the dust removal funnel through the mutual collision of the filler balls 73 and the washing of the spray liquid, and the mutual collision of the filler balls 73 can also serve the purpose of cleaning the filler balls 73, so that the dust-containing gas and the solution are fully Contact completes the dust removal process.

在另一种具体的方案中,湿式振弦栅除尘部分包括射流室8、振弦栅10和振弦栅管路13,射流室8包括气体进入腔和射流器9,射流器9包括文氏管91和设置在文氏管91内的第二喷嘴92,文氏管 91包括依次连接且一体成型的吸气室911、喉管912和扩散管913,振弦栅10的结构如图4所示,气体进入腔一端与填料室7的上端连接,气体进入腔的另一端与文氏管91的吸气室911连接,文氏管91的扩散管913与振弦栅管路13连接,第二喷嘴92连接有第二自动喷雾系统,振弦栅管路13与文氏管91的扩散管913连接的一端内设有多层振弦栅10,前后相邻设置的振弦栅10的振弦丝互相垂直。In another specific scheme, the dust removal part of the wet vibrating wire grid includes a jet chamber 8, a vibrating wire grid 10 and a vibrating wire grid pipeline 13, the jet chamber 8 includes a gas inlet chamber and an ejector 9, and the ejector 9 includes a venturi The tube 91 and the second nozzle 92 arranged in the venturi tube 91, the venturi tube 91 includes a suction chamber 911, a throat tube 912 and a diffuser tube 913 which are sequentially connected and integrally formed. The structure of the vibrating wire grid 10 is shown in Figure 4 As shown, one end of the gas inlet chamber is connected to the upper end of the packing chamber 7, the other end of the gas inlet chamber is connected to the suction chamber 911 of the venturi tube 91, and the diffusion tube 913 of the venturi tube 91 is connected to the vibrating wire grid pipeline 13. Two nozzles 92 are connected with the second automatic spraying system, and the end where the vibrating wire grid pipeline 13 is connected with the diffusion pipe 913 of the Venturi tube 91 is provided with a multi-layer vibrating wire grid 10, and the vibrating wire grid 10 adjacent to the front and back is provided with a vibrating wire grid 10 The strings are perpendicular to each other.

沿风流流动方向,振弦栅管路13在振弦栅10的下方由前至后依次设置有除尘水斗11和除雾水斗12;振弦栅管路13与抽出式风机15的连接位置设置有风机排水管14。Along the wind flow direction, the vibrating wire grid pipeline 13 is provided with a dust removal bucket 11 and a demisting bucket 12 from front to back under the vibration wire grid 10; A fan drain pipe 14 is provided.

更具体的方案中,振弦栅10横截面设计为半径为0.28m的圆形,振弦栅管路13尺寸要稍大于振弦栅10尺寸,半径设计为0.29m。振弦栅10过滤材料选择直径是0.15~0.2mm的合金钢丝,振弦丝间距为1.5mm。振弦栅10结构示意图如图4所示,安装时,相邻两块振弦栅10的振弦丝要前纵后横布置,使相邻振弦栅10上的振弦丝互相垂直。振弦栅10层数为8层,在滤尘的同时,也起着除雾的作用,脱水部分采用振弦栅10除雾,在振弦栅管路13与抽出式风机15的连接位置设置风机排水管14,防止气流带出的水进入抽出式风机15。In a more specific solution, the cross-section of the vibrating wire grid 10 is designed to be a circle with a radius of 0.28m, the size of the vibrating wire grid pipeline 13 is slightly larger than that of the vibrating wire grid 10, and the radius is designed to be 0.29m. The filter material of the vibrating wire grid 10 is an alloy steel wire with a diameter of 0.15-0.2 mm, and the distance between the vibrating wires is 1.5 mm. The schematic diagram of the structure of the vibrating wire grid 10 is shown in Figure 4. During installation, the vibrating wires of two adjacent vibrating wire grids 10 should be arranged vertically at the front and horizontally at the rear, so that the vibrating wires on adjacent vibrating wire grids 10 are perpendicular to each other. The 10 layers of the vibrating wire grid are 8 layers, which also play the role of defogging while filtering dust. The dehydration part uses the vibrating wire grid 10 to defog, and the fan is installed at the connection position between the vibrating wire grid pipeline 13 and the draw-out fan 15 The drain pipe 14 prevents the water brought out by the airflow from entering the draw-out fan 15 .

射流器9包括文氏管91和设置在文氏管91内的第二喷嘴92,有压水流从第二喷嘴92以极高速度射出,使文氏管吸气室911压力降低形成负压卷吸含尘空气,含有较小颗粒煤尘的气流与液滴在文氏管喉口入口段及喉管912内充分混合(气体中尘粒与液滴凝聚成较大颗粒),气液混合体通过文氏管扩散管 913排出,其速度减慢,压力增强,形成强力喷射流以一定速度均匀覆盖振弦栅10的全部断面,如图3所示。The ejector 9 includes a venturi tube 91 and a second nozzle 92 arranged in the venturi tube 91. The pressurized water flow is ejected from the second nozzle 92 at a very high speed, so that the pressure in the suction chamber 911 of the venturi tube is reduced to form a negative pressure coil. Dust-laden air is sucked, and the airflow containing smaller particles of coal dust and liquid droplets are fully mixed in the throat inlet section of the Venturi tube and the throat 912 (the dust particles and liquid droplets in the gas condense into larger particles), and the gas-liquid mixture It is discharged through the Venturi diffuser tube 913, its speed is slowed down, and the pressure is increased to form a powerful jet flow that evenly covers the entire section of the vibrating wire grid 10 at a certain speed, as shown in FIG. 3 .

采用上述结构,首先在粉尘颗粒与振弦栅10接触前,通过高压喷雾对其润湿,一部分较大的粉尘颗粒直接被水滴捕捉,进行初步除尘,另一部分粉尘被振弦栅10捕获。当含有粉尘的空气流经振弦栅10时,粉尘遇到振弦丝上水膜拦截而滞留下来,而且振弦栅10的振弦丝在气流作用产生高频率的震动,加强了水雾粒与含尘空气中粉尘颗粒之间的凝聚作用,从而提高对微细粉尘的捕尘效率。一部分粉尘被振弦栅10上的液体薄膜所捕获,然后被振弦丝上的水滴吸附,由于自身重力沉降并汇集成水流,还能起到清洗振弦栅10的作用。湿润粉尘粒子和水雾随水流分别流向除尘水斗11和除雾水斗12内,净化后的空气流向抽出式风机15。With the above structure, before the dust particles come into contact with the vibrating wire grid 10, they are wetted by high-pressure spraying, some of the larger dust particles are directly captured by the water droplets for preliminary dust removal, and the other part of the dust is captured by the vibrating wire grid 10. When the air containing dust flows through the vibrating wire grid 10, the dust encounters the water film on the vibrating wire and intercepts it and stays, and the vibrating wire of the vibrating wire grid 10 generates high-frequency vibrations under the action of the air flow, which strengthens the water mist particles. Coagulation with dust particles in dusty air, thereby improving the dust collection efficiency of fine dust. Part of the dust is captured by the liquid film on the vibrating wire grid 10, and then absorbed by the water droplets on the vibrating wire. Due to its own gravity, it settles and collects into a water flow, which can also play a role in cleaning the vibrating wire grid 10. The wet dust particles and water mist flow into the dust removal bucket 11 and the mist removal bucket 12 respectively along with the water flow, and the purified air flows to the extraction fan 15 .

填料室7和射流室8内的第一喷嘴74和第二喷嘴92均连接有一套自动喷雾系统,自动喷雾系统包括水阀门、水质过滤器、加压装置、测量装置和电动球阀,将水阀门、水质过滤器、加压装置、测量装置、电动球阀和第一喷嘴74/第二喷嘴92经由连接管路依次连接,由于电动球阀上安装传感器,可以对环境进行自动判断,当有含尘气流经过时,实现自动控制喷雾功能。测量装置采用SGS型双功能高压水表,水质过滤器采用GCQ-3型水质过滤器,加压装置采用BP-75/12型矿用喷雾泵,各装置使用管径为25mm 高压胶管采用快速接头连接方式连接。第二喷嘴92选用2~4个SD304实心锥形喷嘴,使用时第二喷嘴92 将水雾化,流出第二喷嘴92后在高速含尘气流的冲击下再次进行雾化,从而实现二次雾化;第一喷嘴74 选择高压喷雾喷嘴,使填料球73可以充分浸润。The first nozzle 74 and the second nozzle 92 in the packing chamber 7 and the jet chamber 8 are all connected with a set of automatic spraying system, and the automatic spraying system includes a water valve, a water quality filter, a pressurizing device, a measuring device and an electric ball valve, and the water valve , water quality filter, pressurizing device, measuring device, electric ball valve and the first nozzle 74/second nozzle 92 are connected sequentially through the connecting pipeline. Since the sensor is installed on the electric ball valve, the environment can be automatically judged. When there is dusty airflow When passing, the automatic control spray function is realized. The measuring device adopts SGS type dual-function high-pressure water meter, the water quality filter adopts GCQ-3 type water quality filter, the pressurizing device adopts BP-75/12 type mining spray pump, and the diameter of each device is 25mm. The high-pressure hose is connected by a quick connector way to connect. The second nozzle 92 uses 2 to 4 SD304 solid cone nozzles. When in use, the second nozzle 92 atomizes the water, and after flowing out of the second nozzle 92, it is atomized again under the impact of the high-speed dust-laden airflow, thereby realizing the secondary fog. The first nozzle 74 selects a high-pressure spray nozzle so that the filler ball 73 can be fully infiltrated.

含尘风流进入除尘器,除尘过程从粗颗粒、细颗粒到微细颗粒依次净化,其包含多级除尘:一级除尘为自激式水浴除尘部分,用重力机理、惯性机理、离心机理对大颗粒粉尘进行捕集;二级除尘为填料除尘部分,用水浴机理、喷淋机理捕集较小颗粒粉尘;三级除尘为湿式振弦栅除尘部分,用振弦栅高效除尘机理捕集呼吸性粉尘。该除尘器处理风量大、除尘效率高,不易堵塞、便于清洗,具有运行稳定,维修方便等优点,在大体不增加除尘系统所占空间大小的情况下除尘效率达到98.6%以上,能有效解决采用一种除尘器除尘效率达不到而采用多级除尘设备又不能满足煤矿井下狭窄的空间、特殊的技术条件以及对于成本的要求的问题,以应对煤矿综掘工作面存在的粉尘产生量大、浓度高等问题。它的实施应用,对存在有害气体或可燃粉尘场所的空气净化技术也具有重要的意义,推广应用具有重大的社会效益和经济效益。The dust-laden air flow enters the dust collector, and the dust removal process is sequentially purified from coarse particles, fine particles to fine particles. Dust is collected; the secondary dust removal is the dust removal part of the filler, and the water bath mechanism and the spraying mechanism capture small particle dust; the third stage dust removal is the wet vibrating wire grid dust removal part, and the vibrating wire grid high-efficiency dust removal mechanism is used to capture respirable dust . The dust collector has the advantages of large air volume, high dust removal efficiency, not easy to block, easy to clean, stable operation, and convenient maintenance. The dust removal efficiency can reach more than 98.6% without increasing the space occupied by the dust removal system. The dust removal efficiency of a dust collector cannot be reached, and the use of multi-stage dust removal equipment cannot meet the narrow space, special technical conditions and cost requirements of the coal mine underground, in order to deal with the large amount of dust generated in the fully mechanized excavation working face of the coal mine. high concentration issues. Its implementation and application is also of great significance to the air purification technology in places with harmful gases or combustible dust, and its promotion and application has great social and economic benefits.

含尘风流由进气口21进入除尘器,从进气室2、S型叶片4、气雾室6、填料室7、射流室8、振弦栅10、风机排水管14经抽出式风机15流出。The dust-laden wind enters the dust collector through the air inlet 21, and passes through the draw-out fan 15 from the air inlet chamber 2, S-shaped blade 4, aerosol chamber 6, packing chamber 7, jet chamber 8, vibrating wire grid 10, and fan drain pipe 14. flow out.

本实用新型提供的一种新型煤矿高效复合式湿式除尘器统的工作原理及过程如下:The working principle and process of a new coal mine high-efficiency composite wet dust collector system provided by the utility model are as follows:

①含尘气流由进气口21进入进气室2,气体断面扩大,大颗粒粉尘由于速度降低,重力沉降,然后转弯,由于惯性碰撞和离心机理,部分粉尘沉落至除尘漏斗3,含尘气体得到粗净化;①The dust-laden air flow enters the air intake chamber 2 from the air inlet 21, and the cross section of the gas expands. Due to the decrease in speed, the large particles of dust settle by gravity, and then turn around. Due to inertial collision and centrifugal mechanism, part of the dust settles to the dust removal funnel 3, and the dust The gas is roughly purified;

②在抽出式风机15的抽吸作用下,气体进入侧的水位下降,流出侧的水位升高,含尘气流冲击液面,激起大量水滴进入S型叶片4,气水充分混合,一部分尘粒被水滴粘附落至除尘漏斗3,一部分细小尘粒流经S型叶片4由于突然转向形成离心力,水滴尘粒甩至除尘漏斗外壁,流向除尘漏斗3;②Under the suction effect of the extraction fan 15, the water level on the gas inlet side drops, and the water level on the outflow side rises, and the dust-laden airflow hits the liquid surface, arousing a large number of water droplets into the S-shaped blade 4, and the gas and water are fully mixed, and a part of the dust The particles are adhered by water droplets and fall to the dust removal funnel 3, some fine dust particles flow through the S-shaped blade 4 due to the sudden turning to form centrifugal force, the water droplets and dust particles are thrown to the outer wall of the dust removal funnel, and flow to the dust removal funnel 3;

③气流由流经S型叶片4的净化室进入气雾室6,气体流动面积扩大,速度突然降低,部分尘粒重力沉降,净化后气体向上流至填料室7;③The air flow enters the aerosol chamber 6 from the purification chamber flowing through the S-shaped blade 4, the gas flow area expands, the speed suddenly decreases, some dust particles settle by gravity, and the purified gas flows upward to the packing chamber 7;

④填料室7中第一喷嘴74向下喷洒含添加剂的喷淋液,非固定的填料球73被喷淋液充分润湿,经润湿的填料球73在气体冲击的作用下上下翻滚、不断碰撞,由于增加了粉尘与喷淋液的接触时间和接触面积,小粒径粉尘被捕集,填料球73上的粉尘由于喷淋液的冲刷和填料球73的相互碰撞落入除尘漏斗3;④ The first nozzle 74 in the stuffing chamber 7 sprays the spray liquid containing additives downwards, the non-fixed stuffing balls 73 are fully wetted by the spraying fluid, and the wetted stuffing balls 73 roll up and down under the impact of the gas, continuously Collision, due to the increase of the contact time and contact area between the dust and the spray liquid, the small particle size dust is captured, and the dust on the filler ball 73 falls into the dust removal funnel 3 due to the washing of the spray liquid and the collision of the filler ball 73;

⑤第二喷嘴92通过文氏管81将水流喷射出,利用射流原理,高速喷雾进一步加速喷雾与振弦栅10 接口处含尘气体的流入,部分粉尘被碰撞、凝聚、沉降,流进除尘水斗中;⑤ The second nozzle 92 sprays the water out through the venturi tube 81. Using the principle of jet flow, the high-speed spray further accelerates the inflow of the dust-containing gas at the interface between the spray and the vibrating wire grid 10, and part of the dust is collided, condensed, and settled, and flows into the dedusting water in the bucket

⑥含尘气流经振弦栅10,在振弦丝振动作用下产生声波,被振弦栅10拦截的同时加速粉尘颗粒凝聚,落入除尘水斗;⑥The dust-laden air flows through the vibrating wire grid 10, and generates sound waves under the action of the vibrating wire vibration, which is intercepted by the vibrating wire grid 10 and accelerates the agglomeration of dust particles, and falls into the dust removal bucket;

⑦振弦栅10在滤尘的同时,也起着除雾的作用,尤其是后几道振弦栅10,主要是为了达到除雾效果,并使其落入除雾水斗12;⑦ The vibrating wire grid 10 also plays the role of demisting while filtering dust, especially the last few vibrating wire grids 10 are mainly to achieve the demisting effect and make it fall into the demisting bucket 12;

⑧在振弦栅管路13与抽出式风机15的连接位置设置有风机排水管14,如图5所示,对气流中的残余水滴进行收集排放,以免水滴被带入抽出式风机15影响其工作性能。⑧ A fan drain pipe 14 is provided at the connection position between the vibrating wire grid pipeline 13 and the draw-out fan 15, as shown in Figure 5, to collect and discharge the residual water droplets in the airflow, so as to prevent the water droplets from being brought into the draw-out fan 15 to affect other work performance.

本实用新型中应用了具体个例对本实用新型的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本实用新型的方法及其核心思想;同时,对于本领域的一般技术人员,依据本实用新型的思想,在具体实施方式及应用范围上均会有改变之处。综上所述,本说明书内容不应理解为对本实用新型的限制。In the utility model, specific examples have been applied to explain the principle and implementation of the utility model, and the descriptions of the above examples are only used to help understand the method of the utility model and its core idea; meanwhile, for those of ordinary skill in the art , according to the idea of the utility model, there will be changes in the specific implementation and application range. To sum up, the contents of this specification should not be understood as limiting the utility model.

Claims (4)

1.一种新型煤矿高效复合式湿式除尘器,其特征在于:所述除尘器包括自激式水浴除尘部分、填料除尘部分和湿式振弦栅除尘部分,所述自激式水浴除尘部分、所述填料除尘部分和所述湿式振弦栅除尘部分由除尘器底部向上顺次连接;所述除尘器包含多级除尘,除尘过程从粗颗粒、细颗粒到微细颗粒依次净化:一级除尘用所述自激式水浴除尘部分对大颗粒粉尘进行捕集,二级除尘用所述填料除尘部分捕集较小颗粒粉尘,三级除尘用所述湿式振弦珊除尘部分捕集呼吸性粉尘。1. A novel coal mine high-efficiency composite wet dust collector is characterized in that: the dust collector includes a self-excited water bath dust removal part, a filler dust removal part and a wet vibrating wire grid dust removal part, the self-excited water bath dust removal part, the The dust removal part of the filler and the dust removal part of the wet vibrating wire grid are sequentially connected upwards from the bottom of the dust collector; The self-excited water bath dedusting part collects large particle dust, the secondary dust removal uses the filler dedusting part to capture smaller particle dust, and the tertiary dedusting uses the wet vibrating string dedusting part to capture respirable dust. 2.根据权利要求1所述的新型煤矿高效复合式湿式除尘器,其特征在于:所述自激式水浴除尘部分包括进气室、除尘漏斗、S型叶片、溢流水箱和气雾室,所述进气室上开有进气口,所述进气室和所述气雾室紧邻并排设置在所述除尘漏斗上方,且所述进气室和所述气雾室均与所述除尘漏斗连通;所述S型叶片水平布置于所述进气室和所述气雾室之间且位于所述除尘漏斗上方,所述S型叶片包括上叶片和下叶片,所述上叶片和所述下叶片之间形成净化室;所述除尘漏斗底部通过第一阀门连接有第一排浆管,所述除尘漏斗侧壁通过第二阀门连接有第一供水管;所述除尘漏斗为可调式漏斗,所述进气室为可调进气室,所述除尘漏斗包括两端相互连接的锥体固定侧壁和锥体调整侧壁,所述进气室包括两端相互连接的柱体固定侧壁和柱体调整侧壁,所述锥体调整侧壁的上端与所述柱体调整侧壁的下端连接,所述锥体调整侧壁和所述柱体调整侧壁为可伸展侧壁,所述锥体调整侧壁通过支撑件连接有调节手把;所述溢流水箱设置在所述除尘漏斗外侧并通过溢流开口与所述除尘漏斗连通,所述溢流水箱上部设有连通所述溢流水箱和所述气雾室的通气室,所述溢流水箱底部通过第三阀门连接有第二排浆管,所述溢流水箱侧壁通过第四阀门连接有第二供水管,所述溢流水箱内设有水位监测器。2. The new high-efficiency composite wet dust collector for coal mine according to claim 1, characterized in that: the self-excited water bath dedusting part includes an air inlet chamber, a dust removal funnel, an S-shaped blade, an overflow water tank and an aerosol chamber, and the There is an air inlet on the air inlet chamber, and the air inlet chamber and the aerosol chamber are arranged side by side above the dust removal funnel, and both the air inlet chamber and the aerosol chamber are connected to the dust removal funnel Communication; the S-shaped blade is arranged horizontally between the air inlet chamber and the aerosol chamber and above the dust removal funnel, the S-shaped blade includes an upper blade and a lower blade, and the upper blade and the A clean room is formed between the lower blades; the bottom of the dust removal funnel is connected to the first slurry discharge pipe through the first valve, and the side wall of the dust removal funnel is connected to the first water supply pipe through the second valve; the dust removal funnel is an adjustable funnel , the air inlet chamber is an adjustable air inlet chamber, the dust removal funnel includes a cone fixed side wall and a cone adjustment side wall connected at both ends, and the air inlet chamber includes a cylinder fixed side connected at both ends The wall and the cylinder adjustment side wall, the upper end of the cone adjustment side wall is connected to the lower end of the cylinder adjustment side wall, the cone adjustment side wall and the cylinder adjustment side wall are stretchable side walls, The adjustment side wall of the cone is connected with an adjustment handle through a support; the overflow water tank is arranged outside the dust removal funnel and communicated with the dust removal funnel through an overflow opening; The overflow water tank and the ventilation chamber of the aerosol chamber, the bottom of the overflow water tank is connected with the second slurry discharge pipe through the third valve, the side wall of the overflow water tank is connected with the second water supply pipe through the fourth valve, A water level monitor is provided in the overflow water tank. 3.根据权利要求2所述的新型煤矿高效复合式湿式除尘器,其特征在于:所述填料除尘部分包括填料室、填料层、填料上筛板、填料下筛板,所述填料室与所述气雾室连通,所述填料上筛板和所述填料下筛板分别设置在所述填料室的上下两端,所述填料层设置于所述填料上筛板和所述填料下筛板之间,所述填料上筛板上设置有第一喷嘴,所述第一喷嘴连接有第一自动喷雾系统。3. The new high-efficiency composite wet dust collector for coal mine according to claim 2, characterized in that: the filler dedusting part includes a filler chamber, a filler layer, an upper sieve plate for filler, and a lower sieve plate for filler, and the filler chamber and the The aerosol chamber is connected, the upper and lower sieve plates of the packing are respectively arranged at the upper and lower ends of the packing chamber, and the packing layer is arranged on the upper sieve plate of the packing and the lower sieve plate of the packing Between, a first nozzle is arranged on the upper sieve plate of the filler, and the first nozzle is connected with a first automatic spraying system. 4.根据权利要求1所述的新型煤矿高效复合式湿式除尘器,其特征在于:所述湿式振弦栅除尘部分包括射流室、振弦栅和振弦栅管路,所述射流室包括气体进入腔和射流器,所述射流器包括文氏管和设置在所述文氏管内的第二喷嘴,所述文氏管包括依次连接且一体成型的吸气室、喉管和扩散管,所述气体进入腔一端与所述填料室的上端连接,所述气体进入腔的另一端与所述吸气室连接,所述扩散管与所述振弦栅管路连接,所述第二喷嘴连接有第二自动喷雾系统,所述振弦栅管路与所述扩散管连接的一端内设有多层所述振弦栅,前后相邻设置的所述振弦栅的振弦丝互相垂直;沿风流流动方向,所述振弦栅管路在所述振弦栅的下方由前至后依次设置有除尘水斗和除雾水斗;所述振弦栅管路与抽出式风机的连接位置设置有风机排水管。4. The new coal mine high-efficiency composite wet dust collector according to claim 1, characterized in that: the wet vibrating wire grid dedusting part includes a jet chamber, a vibrating wire grid and a vibrating wire grid pipeline, and the jet chamber includes a gas Into the chamber and the ejector, the ejector includes a venturi tube and a second nozzle arranged in the venturi tube, the venturi tube includes a suction chamber, a throat and a diffuser tube that are sequentially connected and integrally formed, so One end of the gas inlet chamber is connected to the upper end of the packing chamber, the other end of the gas inlet chamber is connected to the suction chamber, the diffusion pipe is connected to the vibrating wire grid pipeline, and the second nozzle is connected to There is a second automatic spraying system, the end of the vibrating wire grid pipeline connected to the diffusion pipe is provided with multiple layers of the vibrating wire grids, and the vibrating wires of the vibrating wire grids arranged adjacent to each other are perpendicular to each other; Along the wind flow direction, the vibrating wire grid pipeline is provided with a dust removal water bucket and a demist water bucket in sequence from front to back under the vibration wire grid; A fan drain pipe is provided.
CN201720884364.XU 2017-07-20 2017-07-20 A kind of New Coal Mine efficient composite wet scrubber Expired - Fee Related CN207445851U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110107339A (en) * 2019-04-24 2019-08-09 中南大学 Drilling and blasting method tunneling fast dust-removing device and method
CN112808478A (en) * 2020-12-30 2021-05-18 浙江工业大学 Device and method for synergistically enhancing double-fluid atomization performance

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110107339A (en) * 2019-04-24 2019-08-09 中南大学 Drilling and blasting method tunneling fast dust-removing device and method
CN110107339B (en) * 2019-04-24 2021-07-09 中南大学 Fast dust removal device and method for tunnel excavation by drilling and blasting method
CN112808478A (en) * 2020-12-30 2021-05-18 浙江工业大学 Device and method for synergistically enhancing double-fluid atomization performance

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