CN108479198B - Dust remover and dust removing equipment - Google Patents
Dust remover and dust removing equipment Download PDFInfo
- Publication number
- CN108479198B CN108479198B CN201810597335.4A CN201810597335A CN108479198B CN 108479198 B CN108479198 B CN 108479198B CN 201810597335 A CN201810597335 A CN 201810597335A CN 108479198 B CN108479198 B CN 108479198B
- Authority
- CN
- China
- Prior art keywords
- gas
- dust
- baffle
- cylinder
- dust collector
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/40—Combinations of devices covered by groups B01D45/00 and B01D47/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D51/00—Auxiliary pretreatment of gases or vapours to be cleaned
- B01D51/02—Amassing the particles, e.g. by flocculation
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
本发明提供了一种除尘器及除尘设备,涉及除尘工艺设备技术领域,该除尘器,包括气体进口和气体出口,气体进口向气体出口方向,除尘器包括顺次设置的喷气管机构、挡板、筒体、旋风分离器和风机;喷气管机构的出风口以及筒体的进风口均朝向挡板,且喷气管机构的出风口到挡板的距离小于筒体的进风口到挡板的距离;旋风分离器设置在筒体和风机之间,旋风分离器的进风口与筒体连通,风机的吸力作用于旋风分离器的出风口,以使待处理气体沿气体进口向气体出口方向运动;还包括加湿装置,加湿装置用于对从喷气管机构内喷出的气体进行加湿。该除尘器能够达到更高效率、除尘粒径更小且不存在短路。
The invention provides a dust collector and dust removal equipment, and relates to the technical field of dust removal process equipment. The dust collector includes a gas inlet and a gas outlet. The gas inlet is directed toward the gas outlet. The dust collector includes a jet pipe mechanism and a baffle arranged in sequence. , cylinder, cyclone separator and fan; the air outlet of the jet tube mechanism and the air inlet of the cylinder are all facing the baffle, and the distance from the air outlet of the jet tube mechanism to the baffle is smaller than the distance from the air inlet of the cylinder to the baffle ; The cyclone separator is arranged between the cylinder and the fan, the air inlet of the cyclone separator is connected with the cylinder, and the suction force of the fan acts on the air outlet of the cyclone separator, so that the gas to be treated moves along the gas inlet toward the gas outlet; It also includes a humidification device, which is used to humidify the gas ejected from the jet pipe mechanism. The dust collector can achieve higher efficiency, smaller dust particle size and no short circuits.
Description
技术领域Technical field
本发明涉及除尘工艺设备技术领域,尤其是涉及一种除尘器及除尘设备。The present invention relates to the technical field of dust removal process equipment, and in particular, to a dust collector and dust removal equipment.
背景技术Background technique
旋风除尘器是除尘装置的一类。除尘机理是使含尘气流作旋转运动,借助于离心力将尘粒从气流中分离并捕集于器壁,再借助重力作用使尘粒落入灰斗。Cyclone dust collector is a type of dust removal device. The dust removal mechanism is to make the dust-containing air flow rotate, use centrifugal force to separate the dust particles from the air flow and capture them on the wall, and then use gravity to make the dust particles fall into the ash hopper.
现有的旋风除尘器包括进气管、排气管、圆筒体、圆锥体和灰斗组成。旋风除尘器结构简单,易于制造、安装和维护管理,设备投资和操作费用都较低,已广泛用于从气流中分离固体和液体粒子。The existing cyclone dust collector consists of an air inlet pipe, an exhaust pipe, a cylinder, a cone and an ash hopper. Cyclone dust collector has a simple structure, is easy to manufacture, install and maintain, and has low equipment investment and operating costs. It has been widely used to separate solid and liquid particles from airflow.
但是,现有的旋风除尘器存在处理效率低,对于粒径较小的粉尘处理能力弱的问题。However, the existing cyclone dust collector has the problem of low processing efficiency and weak processing ability for dust with smaller particle size.
发明内容Contents of the invention
本发明的目的在于提供一种除尘器及除尘设备,以缓解了现有的旋风除尘器存在处理效率低,对于粒径较小的粉尘处理能力弱的问题。The object of the present invention is to provide a dust collector and dust removal equipment to alleviate the problems of low processing efficiency and weak processing ability for dust with smaller particle size in existing cyclone dust collectors.
第一方面,本发明实施例提供的一种除尘器,包括气体进口和气体出口,所述气体进口向所述气体出口方向,所述除尘器包括顺次设置的喷气管机构、挡板、筒体、旋风分离器和风机;In a first aspect, an embodiment of the present invention provides a dust collector, which includes a gas inlet and a gas outlet. The gas inlet is directed toward the gas outlet. The dust collector includes a jet pipe mechanism, a baffle, and a barrel arranged in sequence. body, cyclone separator and fan;
所述喷气管机构的出风口以及所述筒体的进风口均朝向所述挡板,且所述喷气管机构的出风口到所述挡板的距离小于所述筒体的进风口到所述挡板的距离;The air outlet of the jet tube mechanism and the air inlet of the cylinder are both facing the baffle, and the distance from the air outlet of the jet tube mechanism to the baffle is smaller than the distance from the air inlet of the barrel to the baffle. baffle distance;
所述旋风分离器设置在所述筒体和所述风机之间,所述旋风分离器的进风口与所述筒体连通,所述风机的吸力作用于所述旋风分离器的出风口,以使待处理气体沿所述气体进口向所述气体出口方向运动;The cyclone separator is arranged between the cylinder and the fan, the air inlet of the cyclone separator is connected with the cylinder, and the suction force of the fan acts on the air outlet of the cyclone separator to causing the gas to be treated to move along the gas inlet toward the gas outlet;
还包括加湿装置,所述加湿装置用于对从所述喷气管机构内喷出的气体进行加湿。It also includes a humidification device, which is used to humidify the gas ejected from the jet pipe mechanism.
结合第一方面,本发明实施例提供了第一方面的第一种可能的实施方式,其中,所述除尘器包括外套壳和内套壳,所述内套壳位于所述外套壳内,所述筒体位于所述内套壳内;In conjunction with the first aspect, the embodiment of the present invention provides a first possible implementation of the first aspect, wherein the dust collector includes an outer casing and an inner casing, and the inner casing is located inside the outer casing, so The cylinder is located in the inner casing;
所述内套壳的外壁与所述外套壳的内壁之间具有间隙,所述间隙用于形成静压箱腔体;所述静压箱腔体分别与气体进口和喷气管机构连通。There is a gap between the outer wall of the inner casing and the inner wall of the outer casing, and the gap is used to form a static pressure box cavity; the static pressure box cavity is connected to the gas inlet and the injection pipe mechanism respectively.
结合第一方面的第一种可能的实施方式,本发明实施例提供了第一方面的第二种可能的实施方式,其中,所述喷气管机构包括文丘里管,所述加湿装置包括水箱,所述水箱与所述文丘里管的内壁连通,以使当所述文丘里管内静压减小时,所述水箱内的水被吸入所述文丘里管内。In conjunction with the first possible implementation of the first aspect, the embodiment of the present invention provides a second possible implementation of the first aspect, wherein the jet tube mechanism includes a venturi tube, and the humidification device includes a water tank, The water tank is connected with the inner wall of the venturi tube, so that when the static pressure in the venturi tube decreases, the water in the water tank is sucked into the venturi tube.
结合第一方面的第二种可能的实施方式,本发明实施例提供了第一方面的第三种可能的实施方式,其中,所述文丘里管的数量为多个,多个所述文丘里管均匀地环绕在所述内套壳的外壁与所述外套壳的内壁之间。In combination with the second possible implementation manner of the first aspect, the embodiment of the present invention provides a third possible implementation manner of the first aspect, wherein the number of the venturi tubes is multiple, and the plurality of venturi tubes are The tube surrounds evenly between the outer wall of the inner casing and the inner wall of the outer casing.
结合第一方面,本发明实施例提供了第一方面的第四种可能的实施方式,其中,所述挡板上设置有通孔,所述挡板下方设置有漏斗形的积尘结构,所述积尘结构上设置有出尘口,以使从所述通孔漏下的颗粒物从所述出尘口排出。In conjunction with the first aspect, embodiments of the present invention provide a fourth possible implementation of the first aspect, wherein a through hole is provided on the baffle, and a funnel-shaped dust accumulation structure is provided below the baffle, so The dust accumulation structure is provided with a dust outlet, so that the particles leaked from the through hole can be discharged from the dust outlet.
结合第一方面的第一种可能的实施方式,本发明实施例提供了第一方面的第五种可能的实施方式,其中,所述旋风分离器的数量为多个。In combination with the first possible implementation manner of the first aspect, an embodiment of the present invention provides a fifth possible implementation manner of the first aspect, wherein the number of the cyclones is multiple.
结合第一方面的第五种可能的实施方式,本发明实施例提供了第一方面的第六种可能的实施方式,其中,多个所述旋风分离器环绕设置在所述内套壳的内壁和所述筒体的外壁之间。In combination with the fifth possible implementation manner of the first aspect, the embodiment of the present invention provides a sixth possible implementation manner of the first aspect, wherein a plurality of cyclone separators are arranged around the inner wall of the inner casing. and between the outer wall of the cylinder.
结合第一方面的第六种可能的实施方式,本发明实施例提供了第一方面的第七种可能的实施方式,其中,所述旋风分离器和所述风机之间设置有气体空腔,多个所述旋风分离器的出风口均与所述气体空腔连通,以使所述风机通过所述气体空腔将吸力作用在多个所述旋风分离器的出气口。In combination with the sixth possible implementation manner of the first aspect, the embodiment of the present invention provides a seventh possible implementation manner of the first aspect, wherein a gas cavity is provided between the cyclone separator and the fan, The air outlets of the plurality of cyclone separators are all connected with the gas cavity, so that the fan applies suction force to the air outlets of the plurality of cyclone separators through the gas cavity.
结合第一方面,本发明实施例提供了第一方面的第八种可能的实施方式,其中,所述喷气管机构的出风口的开口方向垂直于所述挡板。Combined with the first aspect, the embodiment of the present invention provides an eighth possible implementation of the first aspect, wherein the opening direction of the air outlet of the jet pipe mechanism is perpendicular to the baffle.
第二方面,本发明实施例提供的一种除尘设备,包括支撑架、粉尘收集装置和上述的除尘器,所述支撑架用于支撑所述除尘器;所述粉尘收集装置用于收集从所述除尘器中排出的粉尘。In a second aspect, an embodiment of the present invention provides a dust removal equipment, including a support frame, a dust collection device and the above-mentioned dust collector. The support frame is used to support the dust collector; the dust collection device is used to collect dust from all dust collectors. The dust discharged from the dust collector.
本发明实施例带来了以下有益效果:The embodiments of the present invention bring the following beneficial effects:
本发明实施例提供的除尘器,包括气体进口和气体出口,所述气体进口向所述气体出口方向,所述除尘器包括顺次设置的喷气管机构、挡板、筒体、旋风分离器和风机;所述喷气管机构的出风口以及所述筒体的进风口均朝向所述挡板,且所述喷气管机构的出风口到所述挡板的距离小于所述筒体的进风口到所述挡板的距离;所述旋风分离器设置在所述筒体和所述风机之间,所述旋风分离器的进风口与所述筒体连通,所述风机的吸力作用于所述旋风分离器的出风口,以使待处理气体沿所述气体进口向所述气体出口方向运动;还包括加湿装置,所述加湿装置用于对从所述喷气管机构内喷出的气体进行加湿。具体原理如下:含尘气体从气体进口进入到喷气管机构后气体速度加大,加湿装置能够对经过喷气管机构的气体进行加湿,水汽捕捉含尘气体中的颗粒物,颗粒聚集变大,从喷气管机构中出来的气体撞击下面挡板,部分颗粒物附着到挡板上,而气体方向改变为水平方向流动。筒体有从下向上的气流,同时在筒体下方形成从下向上的气流,在筒体气流向上流动和喷气管机构中气体水平流动的共同作用下,在筒体下端空间形成旋转气流,部分颗粒物在旋转气流离心力的作用下被分离出来,分离出来的部分颗粒物会与喷气管机构出流的气体混合再次聚集,再次撞击下面挡板,被滞留到挡板上,气体就得到了净化。筒体下方空间的旋转气流同时向上运动进入到筒体中,气体从筒体上部进入到旋风分离器中,在旋风分离器中部分颗粒物被去除,粉尘从粉尘出口排出,气体受到了再一次的净化处理,从而达到高效除尘的目的。因为有水汽的加入,直径较小的灰尘也可以被捕捉,提高了除尘效率。The dust collector provided by the embodiment of the present invention includes a gas inlet and a gas outlet. The gas inlet is in the direction of the gas outlet. The dust collector includes a jet pipe mechanism, a baffle, a cylinder, a cyclone separator, and a jet pipe mechanism arranged in sequence. Fan; the air outlet of the jet tube mechanism and the air inlet of the barrel are both facing the baffle, and the distance from the air outlet of the jet tube mechanism to the baffle is smaller than the distance from the air inlet of the barrel to the baffle. The distance between the baffles; the cyclone separator is arranged between the cylinder and the fan, the air inlet of the cyclone separator is connected to the cylinder, and the suction force of the fan acts on the cyclone The air outlet of the separator allows the gas to be treated to move along the gas inlet toward the gas outlet; it also includes a humidifying device used to humidify the gas ejected from the jet pipe mechanism. The specific principle is as follows: after the dusty gas enters the jet tube mechanism from the gas inlet, the gas speed increases. The humidification device can humidify the gas passing through the jet tube mechanism. The water vapor captures the particles in the dusty gas, and the particles aggregate and become larger. The gas coming out of the trachea mechanism hits the lower baffle, part of the particles adheres to the baffle, and the direction of the gas changes to a horizontal flow. The cylinder has an airflow from bottom to upward, and at the same time, an airflow from bottom to upward is formed below the cylinder. Under the combined action of the upward flow of the cylinder's airflow and the horizontal flow of gas in the jet tube mechanism, a rotating airflow is formed in the space at the lower end of the cylinder, and part of the The particulate matter is separated under the centrifugal force of the rotating air flow. Part of the separated particulate matter will be mixed with the gas flowing out of the jet pipe mechanism and gathered again. It will hit the lower baffle again and be retained on the baffle, whereupon the gas will be purified. The rotating airflow in the space below the cylinder moves upward at the same time and enters the cylinder. The gas enters the cyclone separator from the upper part of the cylinder. In the cyclone separator, part of the particles are removed, the dust is discharged from the dust outlet, and the gas is subjected to another Purification treatment to achieve the purpose of efficient dust removal. Because of the addition of water vapor, dust with smaller diameters can also be captured, improving dust removal efficiency.
本发明实施例提供的除尘设备,包括支撑架、粉尘收集装置和上述的除尘器,所述支撑架用于支撑所述除尘器,以保证除尘器在工作时平稳,减少晃动;所述粉尘收集装置用于收集从所述除尘器中排出的粉尘。含尘气体从气体进口进入到喷气管机构后气体速度加大,加湿装置能够对经过喷气管机构的气体进行加湿,水汽捕捉含尘气体中的颗粒物,颗粒聚集变大,从喷气管机构中出来的气体撞击下面挡板,部分颗粒物附着到挡板上,而气体方向改变为水平方向流动。筒体有从下向上的气流,同时在筒体下方形成从下向上的气流,在筒体气流向上流动和喷气管机构中气体水平流动的共同作用下,在筒体下端空间形成旋转气流,部分颗粒物在旋转气流离心力的作用下被分离出来,分离出来的部分颗粒物会与喷气管机构出流的气体混合再次聚集,再次撞击下面挡板,被滞留到挡板上,气体就得到了净化。筒体下方空间的旋转气流同时向上运动进入到筒体中,气体从筒体上部进入到旋风分离器中,在旋风分离器中部分颗粒物被去除,粉尘从粉尘出口排出,气体受到了再一次的净化处理,从而达到高效除尘的目的。因为有水汽的加入,直径较小的灰尘也可以被捕捉,提高了除尘效率。The dust removal equipment provided by the embodiment of the present invention includes a support frame, a dust collection device and the above-mentioned dust collector. The support frame is used to support the dust collector to ensure that the dust collector is stable during operation and reduces shaking; the dust collection The device is used to collect the dust discharged from the dust collector. After the dusty gas enters the jet tube mechanism from the gas inlet, the gas speed increases. The humidification device can humidify the gas passing through the jet tube mechanism. The water vapor captures the particles in the dusty gas. The particles aggregate and become larger and come out of the jet tube mechanism. The gas hits the baffle below, some particles adhere to the baffle, and the direction of the gas changes to a horizontal flow. The cylinder has an airflow from bottom to upward, and at the same time, an airflow from bottom to upward is formed below the cylinder. Under the combined action of the upward flow of the cylinder's airflow and the horizontal flow of gas in the jet tube mechanism, a rotating airflow is formed in the space at the lower end of the cylinder, and part of the The particulate matter is separated under the centrifugal force of the rotating air flow. Part of the separated particulate matter will be mixed with the gas flowing out of the jet pipe mechanism and gathered again. It will hit the lower baffle again and be retained on the baffle, whereupon the gas will be purified. The rotating airflow in the space below the cylinder moves upward at the same time and enters the cylinder. The gas enters the cyclone separator from the upper part of the cylinder. In the cyclone separator, part of the particles are removed, the dust is discharged from the dust outlet, and the gas is subjected to another Purification treatment to achieve the purpose of efficient dust removal. Because of the addition of water vapor, dust with smaller diameters can also be captured, improving dust removal efficiency.
本发明的其他特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他优点在说明书、权利要求书以及附图中所特别指出的结构来实现和获得。Additional features and advantages of the invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention. The objectives and other advantages of the invention may be realized and attained by the structure particularly pointed out in the written description, claims and appended drawings.
为使本发明的上述目的、特征和优点能更明显易懂,下文特举较佳实施例,并配合所附附图,作详细说明如下。In order to make the above-mentioned objects, features and advantages of the present invention more obvious and understandable, preferred embodiments are given below and described in detail with reference to the accompanying drawings.
附图说明Description of the drawings
为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,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 explain the specific embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings that need to be used in the description of the specific embodiments or the prior art will be briefly introduced below. Obviously, the drawings in the following description The drawings illustrate some embodiments of the present invention. For those of ordinary skill in the art, other drawings can be obtained based on these drawings without exerting any creative effort.
图1为本发明实施例提供的除尘器的示意图;Figure 1 is a schematic diagram of a dust collector provided by an embodiment of the present invention;
图2为本发明实施例提供的除尘器的内部结构示意图;Figure 2 is a schematic diagram of the internal structure of the dust collector provided by the embodiment of the present invention;
图3为本发明实施例提供的除尘器的气流运行示意图;Figure 3 is a schematic diagram of the air flow operation of the dust collector provided by the embodiment of the present invention;
图4为本发明实施例提供的除尘设备的示意图。Figure 4 is a schematic diagram of the dust removal equipment provided by the embodiment of the present invention.
图标:110-气体进口;120-气体出口;210-文丘里管;220-挡板;221-通孔;230-筒体;240-风机;250-水箱;260-旋风分离器;261-粉尘出口;310-外套壳;320-内套壳;400-静压箱腔体;500-积尘结构;510-出尘口;600-气体空腔;710-支撑架;720-粉尘收集装置。Icon: 110-gas inlet; 120-gas outlet; 210-venturi tube; 220-baffle; 221-through hole; 230-cylinder; 240-fan; 250-water tank; 260-cyclone separator; 261-dust Exit; 310-outer shell; 320-inner shell; 400-static pressure box cavity; 500-dust accumulation structure; 510-dust outlet; 600-gas cavity; 710-support frame; 720-dust collection device.
具体实施方式Detailed ways
下面将结合附图对本发明的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,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,都属于本发明保护的范围。The technical solution of the present invention will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are some, not all, of the embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
在本发明的描述中,需要说明的是,如出现术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等,其指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,如出现术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that if the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" appear, ", etc., the orientation or positional relationship indicated is based on the orientation or positional relationship shown in the drawings, which is only for the convenience of describing the present invention and simplifying the description, and does not indicate or imply that the device or element referred to must have a specific orientation. Constructed and operated in specific orientations and therefore not to be construed as limitations of the invention. In addition, the terms “first,” “second,” and “third”, if used, are for descriptive purposes only and are not to be construed as indicating or implying relative importance.
另外,在本发明实施例的描述中,除非另有明确的规定和限定,术语“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In addition, in the description of the embodiments of the present invention, unless otherwise clearly stated and limited, the terms "connected" and "connected" should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or an integral connection. Connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be an internal connection between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood on a case-by-case basis.
如图1-图3所示,本发明实施例提供的除尘器,包括气体进口110和气体出口120,所述气体进口110向所述气体出口120方向,所述除尘器包括顺次设置的喷气管机构、挡板220、筒体230、旋风分离器260和风机240;所述喷气管机构的出风口以及所述筒体230的进风口均朝向所述挡板220,且所述喷气管机构的出风口到所述挡板220的距离小于所述筒体230的进风口到所述挡板220的距离;所述旋风分离器260设置在所述筒体230和所述风机240之间,所述旋风分离器260的进风口与所述筒体230连通,所述风机240的吸力作用于所述旋风分离器260的出风口,以使待处理气体沿所述气体进口110向所述气体出口120方向运动;还包括加湿装置,所述加湿装置用于对从所述喷气管机构内喷出的气体进行加湿。As shown in Figures 1 to 3, the dust collector provided by the embodiment of the present invention includes a gas inlet 110 and a gas outlet 120. The gas inlet 110 is directed toward the gas outlet 120. The dust collector includes spray jets arranged in sequence. The air pipe mechanism, the baffle 220, the barrel 230, the cyclone separator 260 and the fan 240; the air outlet of the jet pipe mechanism and the air inlet of the barrel 230 are all facing the baffle 220, and the air jet pipe mechanism The distance from the air outlet to the baffle 220 is smaller than the distance from the air inlet of the cylinder 230 to the baffle 220; the cyclone separator 260 is provided between the cylinder 230 and the fan 240, The air inlet of the cyclone separator 260 is connected with the barrel 230 , and the suction force of the fan 240 acts on the air outlet of the cyclone separator 260 so that the gas to be treated flows toward the gas along the gas inlet 110 . The outlet 120 moves in the direction; it also includes a humidifying device, which is used to humidify the gas ejected from the jet tube mechanism.
具体原理如下:含尘气体从气体进口110进入到喷气管机构后气体速度加大,加湿装置能够对经过喷气管机构的气体进行加湿,水汽捕捉含尘气体中的颗粒物,颗粒聚集变大,从喷气管机构中出来的气体撞击下面挡板220,部分颗粒物附着到挡板220上,而气体方向改变为水平方向流动。筒体230有从下向上的气流,同时在筒体230下方形成从下向上的气流,在筒体230气流向上流动和喷气管机构中气体水平流动的共同作用下,在筒体230下端空间形成旋转气流,部分颗粒物在旋转气流离心力的作用下被分离出来,分离出来的部分颗粒物会与喷气管机构出流的气体混合再次聚集,再次撞击下面挡板220,被滞留到挡板220上,气体就得到了净化。筒体230下方空间的旋转气流同时向上运动进入到筒体230中,气体从筒体230上部进入到旋风分离器260中,在旋风分离器260中部分颗粒物被去除,粉尘从粉尘出口261排出,气体受到了再一次的净化处理,从而达到高效除尘的目的。因为有水汽的加入,直径较小的灰尘也可以被捕捉,提高了除尘效率。The specific principle is as follows: after the dusty gas enters the jet tube mechanism from the gas inlet 110, the gas speed increases. The humidification device can humidify the gas passing through the jet tube mechanism. The water vapor captures the particles in the dusty gas, and the particles aggregate and become larger. The gas coming out of the jet tube mechanism hits the lower baffle 220, and some particulate matter adheres to the baffle 220, and the direction of the gas changes to a horizontal flow. The cylinder 230 has an air flow from bottom to upward, and at the same time, an air flow from bottom to upward is formed below the cylinder 230. Under the joint action of the upward air flow of the cylinder 230 and the horizontal flow of gas in the jet tube mechanism, a space at the lower end of the cylinder 230 is formed. In the rotating airflow, some particulate matter is separated under the centrifugal force of the rotating airflow. The separated particulate matter will mix with the gas flowing out of the jet pipe mechanism and gather again. It will hit the lower baffle 220 again and be retained on the baffle 220. The gas It was purified. The rotating airflow in the space below the cylinder 230 moves upward at the same time and enters the cylinder 230. The gas enters the cyclone separator 260 from the upper part of the cylinder 230. Some particulate matter is removed in the cyclone separator 260, and the dust is discharged from the dust outlet 261. The gas is purified again to achieve efficient dust removal. Because of the addition of water vapor, dust with smaller diameters can also be captured, improving dust removal efficiency.
除尘器包括外套壳310和内套壳320,所述内套壳320位于所述外套壳310内,所述筒体230固定在内套壳320内。内套壳320的外壁与所述外套壳310的内壁之间具有间隙,所述间隙用于形成静压箱腔体400;所述静压箱腔体400分别与气体进口110和喷气管机构连通。静压箱腔体400能够减少动压、增加静压和稳定气流,它可使送风效果更加理想。具体作用如下:1、可以把部分动压变为静压使风吹得更远;2、可以降低噪音;3、风量均匀分配;4、静压箱可用来减少噪声,又可获得均匀的静压出风,减少动压损失。The dust collector includes an outer shell 310 and an inner shell 320. The inner shell 320 is located in the outer shell 310, and the cylinder 230 is fixed in the inner shell 320. There is a gap between the outer wall of the inner casing 320 and the inner wall of the outer casing 310, and the gap is used to form a static pressure box cavity 400; the static pressure box cavity 400 is connected to the gas inlet 110 and the injection pipe mechanism respectively. . The static pressure box cavity 400 can reduce dynamic pressure, increase static pressure and stabilize air flow, which can make the air supply effect more ideal. The specific functions are as follows: 1. It can convert part of the dynamic pressure into static pressure to make the wind blow farther; 2. It can reduce the noise; 3. The air volume is evenly distributed; 4. The static pressure box can be used to reduce the noise and obtain uniform static pressure. Pressure out the wind and reduce dynamic pressure loss.
喷气管机构可以包括辅助气泵,可以通过气泵提高出射气体的速度。The jet tube mechanism may include an auxiliary air pump, through which the speed of the ejected gas can be increased.
加湿装置可以为雾化器,将水处理生成水雾,然后将水雾向喷气管机构内的气体喷射。The humidification device can be an atomizer, which processes water to generate water mist, and then sprays the water mist toward the gas in the jet pipe mechanism.
优选的,喷气管机构可以包括文丘里管210,所述加湿装置包括水箱250,所述水箱250与所述文丘里管210的内壁连通,以使当所述文丘里管210内静压减小时,所述水箱250内的水被吸入所述文丘里管210内。文丘里管210中心气体流速增大导致管内静压变小,水箱250中水分从水管进入到文丘里管210中心形成水雾,水雾捕捉含尘气体中的颗粒物,颗粒聚集变大,从射流进气管中出来的气体撞击下面挡板220,部分颗粒物附着到挡板220上,而气体方向改变为水平向中心流动。Preferably, the jet tube mechanism may include a venturi tube 210, and the humidification device includes a water tank 250. The water tank 250 is connected to the inner wall of the venturi tube 210, so that when the static pressure in the venturi tube 210 decreases, , the water in the water tank 250 is sucked into the venturi tube 210 . The increase in the gas flow rate in the center of the Venturi tube 210 causes the static pressure in the tube to decrease. The water in the water tank 250 enters from the water pipe into the center of the Venturi tube 210 to form water mist. The water mist captures the particles in the dust-containing gas, and the particles aggregate and become larger. From the jet The gas coming out of the air inlet pipe hits the lower baffle 220, part of the particles adheres to the baffle 220, and the direction of the gas changes to flow horizontally toward the center.
文丘里管210的数量为多个,多个所述文丘里管210均匀地环绕在所述内套壳320的外壁与所述外套壳310的内壁之间。环形的静压箱腔体400内的气体进入到多个文丘里管210内,提高了气体处理的效率。There are multiple venturi tubes 210 , and the plurality of venturi tubes 210 are evenly surrounded between the outer wall of the inner casing 320 and the inner wall of the outer casing 310 . The gas in the annular static pressure box cavity 400 enters the plurality of venturi tubes 210, which improves the efficiency of gas treatment.
挡板220上设置有通孔221,所述挡板220下方设置有漏斗形的积尘结构500,所述积尘结构500上设置有出尘口510,以使从所述通孔221漏下的颗粒物从所述出尘口510排出。随着水分的增多,滞留在挡板220上的颗粒物随着水流入到挡板220的中心圆孔,从中心圆孔掉落到出尘口510排出。积尘结构500为漏斗形的,可以有效的引导颗粒物从下部的出尘口510排出。The baffle 220 is provided with a through hole 221, and a funnel-shaped dust collecting structure 500 is provided below the baffle 220. The dust collecting structure 500 is provided with a dust outlet 510 to allow dust to leak from the through hole 221. The particulate matter is discharged from the dust outlet 510. As the moisture increases, the particles remaining on the baffle 220 flow into the central circular hole of the baffle 220 with the water, and fall from the central circular hole to the dust outlet 510 for discharge. The dust accumulation structure 500 is funnel-shaped and can effectively guide particulate matter to be discharged from the dust outlet 510 at the lower part.
挡板220可以为漏斗形,通孔221位于漏斗形的挡板220最低端,从而可以使挡板220上附着的颗粒物顺着挡板从通孔221落下。The baffle 220 may be funnel-shaped, and the through hole 221 is located at the lowest end of the funnel-shaped baffle 220, so that the particles attached to the baffle 220 can fall down from the through hole 221 along the baffle.
旋风分离器260的数量为多个,多个所述旋风分离器260环绕设置在所述内套壳320的内壁和所述筒体230的外壁之间。合理利用空间,增加旋风分离器260的数量,提高气体处理的效率。There are multiple cyclone separators 260 , and the plurality of cyclone separators 260 are arranged around the inner wall of the inner casing 320 and the outer wall of the barrel 230 . Make rational use of space, increase the number of cyclone separators 260, and improve the efficiency of gas treatment.
旋风分离器260和所述风机240之间设置有气体空腔600,多个所述旋风分离器260的出风口均与所述气体空腔600连通。通过设置气体空腔600,使用一个风机240即可对多个旋风分离器260的出风口产生负压。A gas cavity 600 is provided between the cyclone separator 260 and the fan 240, and the air outlets of multiple cyclone separators 260 are all connected to the gas cavity 600. By providing the gas cavity 600, one fan 240 can be used to generate negative pressure at the air outlets of multiple cyclones 260.
当喷气管机构的出风口的开口方向垂直于所述挡板220,喷气管机构的出风口的开口方向也可以沿筒体外围顺时针或逆时针呈一定的倾斜角度,利于下端出口气流产生切向气流,促进形成旋风。When the opening direction of the air outlet of the jet tube mechanism is perpendicular to the baffle 220, the opening direction of the air outlet of the jet tube mechanism can also be at a certain inclination angle clockwise or counterclockwise along the periphery of the cylinder, which is conducive to the generation of cut-off airflow at the lower end outlet. Towards the airflow, promoting the formation of cyclones.
如图4所述,本发明实施例提供的除尘设备,包括支撑架710、粉尘收集装置720和上述的除尘器,所述支撑架710用于支撑所述除尘器,以保证除尘器在工作时平稳,减少晃动;所述粉尘收集装置720用于收集从所述除尘器中排出的粉尘。含尘气体从气体进口110进入到喷气管机构后气体速度加大,加湿装置能够对经过喷气管机构的气体进行加湿,水汽捕捉含尘气体中的颗粒物,颗粒聚集变大,从喷气管机构中出来的气体撞击下面挡板220,部分颗粒物附着到挡板220上,而气体方向改变为水平方向流动。筒体230有从下向上的气流,同时在筒体230下方形成从下向上的气流,在筒体230气流向上流动和喷气管机构中气体水平流动的共同作用下,在筒体230下端空间形成旋转气流,部分颗粒物在旋转气流离心力的作用下被分离出来,分离出来的部分颗粒物会与喷气管机构出流的气体混合再次聚集,再次撞击下面挡板220,被滞留到挡板220上,气体就得到了净化。筒体230下方空间的旋转气流同时向上运动进入到筒体230中,气体从筒体230上部进入到旋风分离器260中,在旋风分离器260中部分颗粒物被去除,粉尘从粉尘出口261排出,气体受到了再一次的净化处理,从而达到高效除尘的目的。因为有水汽的加入,直径较小的灰尘也可以被捕捉,提高了除尘效率。As shown in Figure 4, the dust removal equipment provided by the embodiment of the present invention includes a support frame 710, a dust collection device 720 and the above-mentioned dust collector. The support frame 710 is used to support the dust collector to ensure that the dust collector is in operation. Stable and reducing shaking; the dust collection device 720 is used to collect dust discharged from the dust collector. After the dusty gas enters the jet tube mechanism from the gas inlet 110, the gas speed increases. The humidification device can humidify the gas passing through the jet tube mechanism. The water vapor captures the particles in the dusty gas, and the particles aggregate and become larger. From the jet tube mechanism The outgoing gas hits the lower baffle 220, part of the particles adheres to the baffle 220, and the direction of the gas changes to a horizontal flow. The cylinder 230 has an air flow from bottom to upward, and at the same time, an air flow from bottom to upward is formed below the cylinder 230. Under the joint action of the upward air flow of the cylinder 230 and the horizontal flow of gas in the jet tube mechanism, a space at the lower end of the cylinder 230 is formed. In the rotating airflow, some particulate matter is separated under the centrifugal force of the rotating airflow. The separated particulate matter will mix with the gas flowing out of the jet pipe mechanism and gather again. It will hit the lower baffle 220 again and be retained on the baffle 220. The gas It was purified. The rotating airflow in the space below the cylinder 230 moves upward at the same time and enters the cylinder 230. The gas enters the cyclone separator 260 from the upper part of the cylinder 230. Some particulate matter is removed in the cyclone separator 260, and the dust is discharged from the dust outlet 261. The gas is purified again to achieve efficient dust removal. Because of the addition of water vapor, dust with smaller diameters can also be captured, improving dust removal efficiency.
最后应说明的是:以上所述实施例,仅为本发明的具体实施方式,用以说明本发明的技术方案,而非对其限制,本发明的保护范围并不局限于此,尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,其依然可以对前述实施例所记载的技术方案进行修改或可轻易想到变化,或者对其中部分技术特征进行等同替换;而这些修改、变化或者替换,并不使相应技术方案的本质脱离本发明实施例技术方案的精神和范围,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应所述以权利要求的保护范围为准。Finally, it should be noted that the above-mentioned embodiments are only specific implementations of the present invention and are used to illustrate the technical solutions of the present invention rather than to limit them. The protection scope of the present invention is not limited thereto. Although refer to the foregoing The embodiments illustrate the present invention in detail. Those of ordinary skill in the art should understand that any person familiar with the technical field can still modify the technical solutions recorded in the foregoing embodiments within the technical scope disclosed by the present invention. It may be easy to think of changes, or equivalent substitutions of some of the technical features; and these modifications, changes or substitutions do not cause the essence of the corresponding technical solutions to deviate from the spirit and scope of the technical solutions of the embodiments of the present invention, and they should all be included in the present invention. within the scope of protection. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810597335.4A CN108479198B (en) | 2018-06-11 | 2018-06-11 | Dust remover and dust removing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810597335.4A CN108479198B (en) | 2018-06-11 | 2018-06-11 | Dust remover and dust removing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108479198A CN108479198A (en) | 2018-09-04 |
| CN108479198B true CN108479198B (en) | 2023-10-27 |
Family
ID=63342643
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810597335.4A Active CN108479198B (en) | 2018-06-11 | 2018-06-11 | Dust remover and dust removing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108479198B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110018088A (en) * | 2019-03-05 | 2019-07-16 | 中国矿业大学 | A kind of opencut dust dirt environment simulation test system and method |
| CN109806674B (en) * | 2019-03-28 | 2024-03-15 | 南华大学 | Solid-gas separation device for pneumatic conveying or ventilation system |
| CN110076011B (en) * | 2019-05-20 | 2024-04-26 | 兰州大学 | Anti-back mixing cyclone dust removal device and cyclone dust removal system |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1162553A (en) * | 1997-08-21 | 1999-03-05 | Toyota Motor Corp | Exhaust gas purification device for internal combustion engine |
| CN101720248A (en) * | 2007-05-24 | 2010-06-02 | 皇家器具有限公司 | Dual stage cyclonic vacuum cleaner |
| CN103785265A (en) * | 2014-02-24 | 2014-05-14 | 深圳市泓耀环保有限公司 | Novel indoor air purification device |
| CN204017604U (en) * | 2014-02-24 | 2014-12-17 | 深圳广昌达环境科学有限公司 | Novel indoor air purifier |
| CN104645768A (en) * | 2015-02-10 | 2015-05-27 | 北京中能诺泰节能环保技术有限责任公司 | Wet-type cyclone dust removal device |
| CN104906896A (en) * | 2015-06-25 | 2015-09-16 | 王博 | Cloud type dust removal system |
| CN105830167A (en) * | 2014-03-03 | 2016-08-03 | 未来与挑战株式会社 | Containment filtered venting system used for nuclear power plant |
| CN207085602U (en) * | 2017-06-07 | 2018-03-13 | 南昌航空大学 | A kind of efficiently anti-suck venturi cyclone dust collectors |
-
2018
- 2018-06-11 CN CN201810597335.4A patent/CN108479198B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH1162553A (en) * | 1997-08-21 | 1999-03-05 | Toyota Motor Corp | Exhaust gas purification device for internal combustion engine |
| CN101720248A (en) * | 2007-05-24 | 2010-06-02 | 皇家器具有限公司 | Dual stage cyclonic vacuum cleaner |
| CN103785265A (en) * | 2014-02-24 | 2014-05-14 | 深圳市泓耀环保有限公司 | Novel indoor air purification device |
| CN204017604U (en) * | 2014-02-24 | 2014-12-17 | 深圳广昌达环境科学有限公司 | Novel indoor air purifier |
| CN105830167A (en) * | 2014-03-03 | 2016-08-03 | 未来与挑战株式会社 | Containment filtered venting system used for nuclear power plant |
| CN104645768A (en) * | 2015-02-10 | 2015-05-27 | 北京中能诺泰节能环保技术有限责任公司 | Wet-type cyclone dust removal device |
| CN104906896A (en) * | 2015-06-25 | 2015-09-16 | 王博 | Cloud type dust removal system |
| CN207085602U (en) * | 2017-06-07 | 2018-03-13 | 南昌航空大学 | A kind of efficiently anti-suck venturi cyclone dust collectors |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108479198A (en) | 2018-09-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108479198B (en) | Dust remover and dust removing equipment | |
| CN103622642A (en) | Dust collector dust cup without suction loss | |
| CN206009023U (en) | A kind of bipyramid cylinder cyclone dust collector | |
| CN116920553B (en) | Flue gas dust-settling treatment device for coal-fired industrial furnace | |
| CN110075652A (en) | A kind of grain drier exhaust gas Combined dust-cleaning apparatus | |
| CN102600994A (en) | Electric spraying cyclone dust collector and application thereof | |
| CN208466198U (en) | A kind of introducing-type cyclone separator | |
| CN108619794B (en) | Dust remover and dust removing equipment | |
| CN207520098U (en) | Dust collect plant and dust catcher | |
| CN111632437A (en) | Centrifugal separation device | |
| CN207119200U (en) | A kind of cyclone type fume dust remover | |
| CN203364204U (en) | Swirling-flow type range hood | |
| CN110124423B (en) | A new energy-saving air purifier | |
| CN205537153U (en) | Environmental protection low energy consumption dust removal terminal | |
| CN208115332U (en) | A kind of environment-protecting industrial exhaust-gas treatment cyclone dust collectors | |
| CN205287979U (en) | Compound dust remover of pipe bag | |
| CN208482198U (en) | Deduster and cleaner | |
| CN104128058A (en) | Vertical electrical dust collector integrating gravity and cyclone dust removal | |
| CN212491953U (en) | Centrifugal separation device | |
| CN208465513U (en) | A smoldering furnace waste gas treatment device | |
| CN208482135U (en) | Deduster and cleaner | |
| CN204193723U (en) | Eddy flow air intake twin-stage purifying dust-removing device | |
| CN116440635A (en) | A kind of separator combined with spray washing and cyclone centrifugation and its separation method | |
| CN211025633U (en) | Cyclone industrial dust removal equipment | |
| CN103127796A (en) | Negative-pressure-absorption discharge-reduction system of tail gas in titanium tetrachloride production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |