CN205288757U - A draw and penetrate atomizing device for opening wide space dust is administered - Google Patents
A draw and penetrate atomizing device for opening wide space dust is administered Download PDFInfo
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Abstract
本实用新型涉及一种用于敞开空间粉尘治理的引射雾化装置,包括沿气体输出向同轴依次设置的吸气室、喷射管、混合室、扩散室和雾化器,其中吸气室为输入口大于输出口的缩径腔体,扩散室为输入口小于输出口的扩径腔体,混合室两端分别与吸气室输出口及扩散室输入口连接,喷射管的出口管径收缩并插置入吸气室内,雾化器为一个安装在扩散室上的带有螺旋通道的通管喷嘴。本实用新型利用流体碰撞雾化原理,通过液体在喷射时将周围气体吸入,并将液体的动能传递给气体,带动气体高速流动,同时在扩散室中形成“液包气”,最终由雾化器喷出,产生更小雾滴并继续在空间中混合吸收,由此达到了混合雾化吸收、治理粉尘的效果。
The utility model relates to an injection atomization device for dust control in an open space, which comprises an air suction chamber, a spray pipe, a mixing chamber, a diffusion chamber and an atomizer which are sequentially arranged coaxially along the gas output direction, wherein the air suction chamber It is a reduced-diameter cavity whose input port is larger than the output port, and the diffusion chamber is an enlarged-diameter cavity whose input port is smaller than the output port. The two ends of the mixing chamber are respectively connected with the output port of the suction chamber and the input port of the diffusion chamber. Shrunken and inserted into the suction chamber, the atomizer is a through-pipe nozzle with a spiral channel mounted on the diffuser chamber. The utility model utilizes the principle of fluid collision atomization, sucks the surrounding gas through the liquid when it is sprayed, and transfers the kinetic energy of the liquid to the gas to drive the gas to flow at a high speed. It is sprayed out by the device to produce smaller mist droplets and continue to mix and absorb in the space, thus achieving the effect of mixed atomization absorption and dust control.
Description
技术领域technical field
本实用新型属于环保设施技术领域,涉及一种用于敞开空间粉尘治理的装置,特别是一种利用液体射流产生负压并且能够雾化液体的引射雾化装置。The utility model belongs to the technical field of environmental protection facilities, and relates to a device for controlling dust in an open space, in particular to an injection atomization device which uses liquid jets to generate negative pressure and can atomize liquid.
背景技术Background technique
工业粉尘排放是造成区域环境大气污染及雾霾天气的重要原因,而大型机加工车间、油漆涂装车间、水泥粉料包装车间、自然通风造粒塔等敞开空间设施的粉尘排放常常造成了周边大气环境的严重污染。传统的敞开空间粉尘治理方法均需要大功率的抽风机、洗涤及吸收等设备,存在着设备投资大、能耗高,运行成本高、治理效果不理想等缺点。Industrial dust emission is an important cause of regional environmental air pollution and smog weather, while the dust emission of large-scale machining workshops, paint coating workshops, cement powder packaging workshops, natural ventilation granulation towers and other open space facilities often cause surrounding pollution. Serious pollution of the atmospheric environment. Traditional open space dust control methods require high-power exhaust fans, washing and absorption equipment, which have the disadvantages of large equipment investment, high energy consumption, high operating costs, and unsatisfactory control effects.
实用新型内容Utility model content
本实用新型的目的在于对现有技术存在的问题加以解决,提供一种用于敞开空间粉尘治理的引射雾化装置,该装置利用流体碰撞雾化原理,可以高效地去除敞开空间设施排放的工业粉尘。The purpose of the utility model is to solve the problems existing in the prior art, and to provide an injection atomization device for dust control in open spaces. industrial dust.
为实现上述发明目的而采用的技术解决方案是这样的:所提供的用于敞开空间粉尘治理的引射雾化装置包括沿气体输出向同轴依次设置的吸气室、喷射管、混合室、扩散室和雾化器,其中,吸气室为一个输入口大于输出口的缩径腔体,扩散室为一个输入口小于输出口的扩径腔体,混合室为一个两端分别与吸气室输出口及扩散室输入口连接的等径腔体,喷射管的出口管径收缩并插置入吸气室内,雾化器的一端贯通安装在扩散室上,为一个带有螺旋通道的通管喷嘴。The technical solution adopted to achieve the above-mentioned invention is as follows: the injection atomization device provided for dust control in an open space includes a suction chamber, an injection pipe, a mixing chamber, Diffusion chamber and atomizer, wherein, the suction chamber is a cavity with a reduced diameter whose input port is larger than the output port, the diffusion chamber is a cavity with an enlarged diameter whose input port is smaller than the output port, and the mixing chamber is a cavity with two ends connected to the suction port respectively. The equal-diameter cavity connected to the output port of the diffusion chamber and the input port of the diffusion chamber, the outlet diameter of the injection pipe is shrunk and inserted into the suction chamber, and one end of the atomizer is installed through the diffusion chamber, which is a through-hole with a spiral channel. Tube nozzle.
上述用于敞开空间粉尘治理的引射雾化装置中,喷射管插置入吸气室内的出口端头距混合室有一定间距,在喷射管上设置有可调节喷射管与混合室之间距离的间距调节部件。In the above ejection atomization device for dust control in open spaces, the outlet end of the injection pipe inserted into the suction chamber has a certain distance from the mixing chamber, and the distance between the injection pipe and the mixing chamber is adjustable. spacing adjustment parts.
上述用于敞开空间粉尘治理的引射雾化装置中,扩散室输出端部具有一段等径内圆周螺纹表面,雾化器输入端部具有一段等径外圆周螺纹表面,扩散室和雾化器通过二者间的螺纹贯通安装在一起。In the above ejection atomization device for dust control in open spaces, the output end of the diffusion chamber has a section of equal-diameter inner-circumferential threaded surface, and the input end of the atomizer has an equal-diameter outer-circumferential threaded surface. The diffusion chamber and the atomizer Installed together through the screw thread between the two.
上述用于敞开空间粉尘治理的引射雾化装置中,雾化器的雾化角度为60°~150°。In the above ejection atomization device for dust control in open spaces, the atomization angle of the atomizer is 60°-150°.
本实用新型结构的工作原理是这样的:喷射管一端与带压水连接,另一端插入吸气室内,吸气室用于吸入周围气体,其内壁和喷射管外壁之间有间隙;混合室与喷射管不接触,喷射管上设置有径向调节部件,可以调节喷射管与混合室之间的距离;喷射管出口管径收缩,用于喷射液体。当装置开始工作时,水从喷射管口高速喷出,在混合管入口处产生负压,气体通过吸气室被带入混合室;在混合室气液混合吸收后进入扩散室,气液混合物在扩散室混合升压后进入雾化器,最后通过雾化器将雾化后的液滴呈一定角度向外喷出。The working principle of the structure of the utility model is as follows: one end of the injection pipe is connected with the pressurized water, and the other end is inserted into the air suction chamber, which is used to inhale the surrounding gas, and there is a gap between the inner wall and the outer wall of the injection pipe; the mixing chamber and the outer wall of the injection pipe The spray pipe is not in contact, and the spray pipe is provided with a radial adjustment component, which can adjust the distance between the spray pipe and the mixing chamber; the diameter of the exit of the spray pipe is contracted to spray liquid. When the device starts to work, water is jetted out at high speed from the injection nozzle, and a negative pressure is generated at the inlet of the mixing tube, and the gas is brought into the mixing chamber through the suction chamber; after the gas-liquid is mixed and absorbed in the mixing chamber, it enters the diffusion chamber, and the gas-liquid mixture After mixed and boosted in the diffusion chamber, it enters the atomizer, and finally the atomized droplets are sprayed out at a certain angle through the atomizer.
与现有技术相比,本实用新型的有益效果如下所述。Compared with the prior art, the beneficial effects of the utility model are as follows.
该引射雾化装置巧妙利用流体碰撞雾化原理,使液体在喷射时将周围气体吸入,并将液体的动能传递给气体,带动气体流动,在保证一定负压的基础上实现最大液气比,从而提高气体的流速,同时在扩散室中形成“液包气”,最终由雾化器喷出,产生更小雾滴并继续在空间中混合吸收,从而达到了混合雾化吸收、治理粉尘的效果。The injection atomization device cleverly utilizes the principle of fluid collision atomization, so that the liquid inhales the surrounding gas when spraying, and transfers the kinetic energy of the liquid to the gas to drive the gas flow, and achieve the maximum liquid-gas ratio on the basis of ensuring a certain negative pressure. , so as to increase the flow rate of the gas, and at the same time form a "gas in liquid" in the diffusion chamber, which is finally sprayed out by the atomizer to produce smaller droplets and continue to mix and absorb in the space, thus achieving mixed atomization absorption and dust control Effect.
本实用新型产品可广泛用于敞开空间(如涂料粉刷车间,油漆车间)和造粒塔中粉尘和有害气体的治理。以应用于造粒塔顶粉尘回收装置为例,在粉尘回收装置中分布若干本实用新型所述引射雾化装置,其喷射方向与尾气流动方向一致,多个引射雾化装置产生的负压能够提高上升含尘气体的流速,同时气液混合物通过雾化器分散后交汇撞击,一同向上喷射并产生混合,从而达到吸收粉尘的目的。本实用新型应用于造粒塔粉尘回收系统中,带动了尾气的流动速度,降低了粉尘回收装置的阻力,不需采用大功率风机为气体提供动能,降低了除尘装置对造粒系统的影响,节能增效显著。The product of the utility model can be widely used in the treatment of dust and harmful gases in open spaces (such as paint painting workshops and paint workshops) and granulation towers. Taking the dust recovery device on the top of the granulation tower as an example, several injection atomization devices described in the present invention are distributed in the dust recovery device, and the injection direction is consistent with the flow direction of the tail gas. The pressure can increase the flow rate of the rising dust-laden gas. At the same time, the gas-liquid mixture is dispersed through the atomizer and then meets and collides. They are sprayed upward together and mixed, so as to achieve the purpose of absorbing dust. The utility model is applied in the dust recovery system of the granulation tower, drives the flow speed of the tail gas, reduces the resistance of the dust recovery device, does not need to use a high-power fan to provide kinetic energy for the gas, and reduces the influence of the dust removal device on the granulation system. Significant energy saving and efficiency enhancement.
附图说明Description of drawings
图1是本实用新型一个具体实施例的结构示意图。Fig. 1 is a schematic structural view of a specific embodiment of the present invention.
图中各数字标号的名称分别是:1-吸气室;2-喷射管;3-混合室;4-扩散室;5-雾化器。The names of the numbers in the figure are: 1-suction chamber; 2-jet pipe; 3-mixing chamber; 4-diffusion chamber; 5-atomizer.
具体实施方式detailed description
参见附图,本实用新型所述的用于敞开空间粉尘治理的引射雾化装置包括沿气体输出向同轴依次设置的吸气室1、喷射管2、混合室3、扩散室4和雾化器5。Referring to the accompanying drawings, the injection atomization device for dust control in open space described in the utility model includes an air suction chamber 1, an injection pipe 2, a mixing chamber 3, a diffusion chamber 4 and a mist Converter 5.
吸气室1为输入口大于输出口的缩径腔体,其输入端口敞开与外界气体相通。混合室3为等径腔体,其两端分别与吸气室1输出口及扩散室4输入口连接。扩散室4为输入口小于输出口的扩径腔体,在其输出端部具有一段用于与雾化器5连接的等径内圆周螺纹表面。雾化器5为一个带有螺旋通道的通管喷嘴,其输入端部具有一段等径外圆周螺纹表面。扩散室4和雾化器5贯通安装,其安装角度与螺纹的螺旋角度吻合,扩散室扩散角在4°~8°,雾化器5的雾化角度在60°~150°之间,喷射管与雾化器的轴线必须同轴。喷射管2插入吸气室1内,喷射管2与吸气室1和混合室3不接触,喷射管2的端部设置有间距调节部件,可以调节喷射管2与混合室3之间的距离。The suction chamber 1 is a reduced-diameter cavity whose input port is larger than the output port, and its input port is open to communicate with the outside air. The mixing chamber 3 is an equal-diameter cavity, and its two ends are respectively connected with the output port of the suction chamber 1 and the input port of the diffusion chamber 4 . The diffusion chamber 4 is an enlarged-diameter cavity with an input port smaller than the output port, and has a section of equal-diameter inner circumferential threaded surface at its output end for connecting with the atomizer 5 . The atomizer 5 is a through-pipe nozzle with a spiral channel, and its input end has a section of equal-diameter outer circumferential threaded surface. Diffusion chamber 4 and atomizer 5 are installed through through, and the installation angle coincides with the helix angle of the screw thread. The axis of the tube and nebulizer must be coaxial. The injection pipe 2 is inserted into the suction chamber 1, the injection pipe 2 is not in contact with the suction chamber 1 and the mixing chamber 3, and the end of the injection pipe 2 is provided with a distance adjusting part, which can adjust the distance between the injection pipe 2 and the mixing chamber 3 .
实际工作中,液体(如水、碱液等)经循环泵提高压力后由喷射管2进入混合室3,喷射管中液体的压力可以在0.1~0.6MPa之间自由调节;从喷射管2喷出的高速液体在流动时,由于液体边界层的粘滞作用,射流液体将气体从吸气室1带入混合室3,在混合室3内产生负压;气体和液体的相对运动,使液体变成不连续的大液滴,气液混合物在混合室3中碰撞、冲击,将能量传递给气体,在扩散室4气液混合物压力升高,气体被压缩,最后由雾化器5将之分散成小液滴并呈一定的角度喷射出去,达到了混合雾化吸收、治理粉尘的效果。In actual work, the liquid (such as water, lye, etc.) enters the mixing chamber 3 from the injection pipe 2 after the pressure is increased by the circulating pump, and the pressure of the liquid in the injection pipe can be adjusted freely between 0.1 and 0.6 MPa; When the high-speed liquid is flowing, due to the viscous effect of the liquid boundary layer, the jet liquid will bring the gas from the suction chamber 1 into the mixing chamber 3, and a negative pressure will be generated in the mixing chamber 3; the relative motion of the gas and the liquid makes the liquid become The gas-liquid mixture collides and impacts in the mixing chamber 3, and transfers energy to the gas. In the diffusion chamber 4, the pressure of the gas-liquid mixture increases, the gas is compressed, and finally dispersed by the atomizer 5 It forms small droplets and sprays them out at a certain angle, achieving the effects of mixed atomization absorption and dust control.
以上所述仅是本实用新型的较佳实施例而已,并非对本实用新型作任何形式上的限制,但凡是未脱离本实用新型技术方案的内容,依据本实用新型的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本实用新型技术方案的范围内。The above descriptions are only preferred embodiments of the present utility model, and are not intended to limit the present utility model in any form. However, any content that does not depart from the technical solution of the present utility model is based on the technical essence of the present utility model. Any simple modifications, equivalent changes and modifications still belong to the scope of the technical solution of the present utility model.
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| CN201521132188.1U CN205288757U (en) | 2015-12-30 | 2015-12-30 | A draw and penetrate atomizing device for opening wide space dust is administered |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
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| RU2636721C1 (en) * | 2016-11-09 | 2017-11-27 | Олег Савельевич Кочетов | Nozzle with parabolic swirler |
| RU2636715C1 (en) * | 2016-11-09 | 2017-11-27 | Олег Савельевич Кочетов | Nozzle for wet dust collection units |
| RU2646912C1 (en) * | 2016-11-09 | 2018-03-12 | Олег Савельевич Кочетов | Nozzle with elliptical swirler |
| RU2656456C1 (en) * | 2017-12-01 | 2018-06-05 | Олег Савельевич Кочетов | Gas scrubber |
| RU2659050C1 (en) * | 2017-11-27 | 2018-06-27 | Олег Савельевич Кочетов | Nozzle for wet dust collecting apparatus |
| RU2659979C1 (en) * | 2017-11-27 | 2018-07-04 | Олег Савельевич Кочетов | Atomizer with parabolic swirler |
| RU2664886C1 (en) * | 2018-02-26 | 2018-08-23 | Олег Савельевич Кочетов | Nozzle with elliptical swirler |
| RU2673047C1 (en) * | 2017-12-01 | 2018-11-21 | Олег Савельевич Кочетов | Conical jet scrubber |
| CN109453586A (en) * | 2018-12-28 | 2019-03-12 | 启明星宇节能科技股份有限公司 | A PM particle capture device |
| CN111530200A (en) * | 2020-05-09 | 2020-08-14 | 宁波奥克斯电气股份有限公司 | an atomizing device |
| RU230719U1 (en) * | 2024-07-16 | 2024-12-18 | Игорь Сергеевич Американцев | Vertical scrubber |
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2015
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2636721C1 (en) * | 2016-11-09 | 2017-11-27 | Олег Савельевич Кочетов | Nozzle with parabolic swirler |
| RU2636715C1 (en) * | 2016-11-09 | 2017-11-27 | Олег Савельевич Кочетов | Nozzle for wet dust collection units |
| RU2646912C1 (en) * | 2016-11-09 | 2018-03-12 | Олег Савельевич Кочетов | Nozzle with elliptical swirler |
| RU2659050C1 (en) * | 2017-11-27 | 2018-06-27 | Олег Савельевич Кочетов | Nozzle for wet dust collecting apparatus |
| RU2659979C1 (en) * | 2017-11-27 | 2018-07-04 | Олег Савельевич Кочетов | Atomizer with parabolic swirler |
| RU2656456C1 (en) * | 2017-12-01 | 2018-06-05 | Олег Савельевич Кочетов | Gas scrubber |
| RU2673047C1 (en) * | 2017-12-01 | 2018-11-21 | Олег Савельевич Кочетов | Conical jet scrubber |
| RU2664886C1 (en) * | 2018-02-26 | 2018-08-23 | Олег Савельевич Кочетов | Nozzle with elliptical swirler |
| CN109453586A (en) * | 2018-12-28 | 2019-03-12 | 启明星宇节能科技股份有限公司 | A PM particle capture device |
| CN111530200A (en) * | 2020-05-09 | 2020-08-14 | 宁波奥克斯电气股份有限公司 | an atomizing device |
| RU230719U1 (en) * | 2024-07-16 | 2024-12-18 | Игорь Сергеевич Американцев | Vertical scrubber |
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