[go: up one dir, main page]

CN108392903A - A kind of double ash bucket inertial dust separators - Google Patents

A kind of double ash bucket inertial dust separators Download PDF

Info

Publication number
CN108392903A
CN108392903A CN201810553610.2A CN201810553610A CN108392903A CN 108392903 A CN108392903 A CN 108392903A CN 201810553610 A CN201810553610 A CN 201810553610A CN 108392903 A CN108392903 A CN 108392903A
Authority
CN
China
Prior art keywords
dust
baffle
ash bucket
dust collector
ash hopper
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.)
Pending
Application number
CN201810553610.2A
Other languages
Chinese (zh)
Inventor
吕薇
吴维峰
高文学
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Harbin University of Science and Technology
Original Assignee
Harbin University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Harbin University of Science and Technology filed Critical Harbin University of Science and Technology
Priority to CN201810553610.2A priority Critical patent/CN108392903A/en
Publication of CN108392903A publication Critical patent/CN108392903A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/08Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

本发明发明一种双灰斗惯性除尘器,入口处采用喷管加速来提高含尘气体的进口流速,使速度达到一个合适的数值,气体经加速后垂直射入除尘器碰撞到第一个阻碍——倾斜挡板。第一次经过碰撞摩擦减速,较大的颗粒粒子被倾斜挡板约束运动方向,进而被减速进入灰斗1,较小的灰尘颗粒随气流转弯进一步减速,由于离心力进入灰斗2。除尘器设置多个截面突变和倾斜挡板,主要是为了增大摩擦,整体上减小流体流速。除尘器总体体积较现有的惯性除尘器大大缩小,可以更加灵活的适应一些狭窄空间。如在大空间使用可并联多个该除尘器。灰斗2左侧设置有压力平衡孔,其作用为平衡灰斗2和外部环境的大气压,改善灰斗2内的流体状态,便于灰尘更好地除去。该惯性除尘器不仅能减少二次扬尘,还减少了气体流动过程中的阻力,也在一定程度上提高了除尘效率。而且入口风压的降低直接减少了风机的功率,达到节约能源的效果。

The invention invents an inertial dust collector with double ash hoppers. The nozzle acceleration is used at the entrance to increase the inlet flow velocity of the dust-laden gas, so that the velocity reaches a suitable value. After the gas is accelerated, it is vertically injected into the dust collector and hits the first obstacle. - Tilted baffles. After the first deceleration by collision and friction, the larger particles are restrained by the inclined baffle in the direction of movement, and then decelerated into the ash hopper 1, and the smaller dust particles are further decelerated with the turning of the airflow, and enter the ash hopper 2 due to centrifugal force. The dust collector is equipped with multiple cross-sectional mutations and inclined baffles, mainly to increase friction and reduce the fluid flow rate as a whole. Compared with the existing inertial dust collector, the overall volume of the dust collector is greatly reduced, and it can be more flexibly adapted to some narrow spaces. If it is used in a large space, multiple dust collectors can be connected in parallel. The left side of the ash hopper 2 is provided with a pressure balance hole, which is used to balance the atmospheric pressure between the ash hopper 2 and the external environment, improve the fluid state in the ash hopper 2, and facilitate better removal of dust. The inertial dust collector can not only reduce the secondary dust, but also reduce the resistance in the process of gas flow, and also improve the dust removal efficiency to a certain extent. Moreover, the reduction of the inlet wind pressure directly reduces the power of the fan, achieving the effect of saving energy.

Description

一种双灰斗惯性除尘器A double ash hopper inertial dust collector

技术领域technical field

本发明涉及环保技术设备领域,具体为一种双灰斗惯性除尘器。The invention relates to the field of environmental protection technical equipment, in particular to an inertial dust collector with double ash hoppers.

背景技术Background technique

目前,公知的惯性除尘器有碰撞式除尘器和回流式除尘器两种,前一种除尘器主要是由一个或几个挡板阻挡气流的前进,使气流中的尘粒分离出来,虽然该形式除尘器气体流动阻力小,但是其除尘效率低。后一种除尘器的特点是把进气流用挡板分割成小股气流,为使任意一股气流都有同样的较小回转半径及较大回转角,可以采用各种挡板结构,最典型的便是百叶挡板,百叶挡板虽然能提高气流急剧转折前的速度,可以有效地提高分离效率,但速度过高会引起已捕集颗粒的二次飞扬。所以,为了克服现有除尘器的二次尘化,气体流动阻力大,除尘效率偏低的不足。因此,本发明提供一种惯性除尘器,对原有的装置改进优化,该惯性除尘器不仅能减少二次扬尘,还减少了气体流动过程中的阻力,也在一定程度上提高了除尘效率。而且入口风压的降低直接减少了风机的功率,达到节约能源的效果。At present, the known inertial dust collectors include impact dust collectors and return dust collectors. The former dust collector mainly uses one or several baffles to block the progress of the airflow, so that the dust particles in the airflow are separated. The gas flow resistance of the form dust collector is small, but its dust removal efficiency is low. The characteristic of the latter type of dust collector is that the intake air flow is divided into small airflows by baffles. In order to make any airflow have the same smaller radius of gyration and larger angle of gyration, various baffle structures can be used. The most typical The most important thing is the louver baffle. Although the louver baffle can increase the speed before the sharp turn of the airflow, it can effectively improve the separation efficiency, but if the speed is too high, it will cause the trapped particles to fly again. Therefore, in order to overcome the secondary dusting of the existing dust collector, the gas flow resistance is large and the dust removal efficiency is low. Therefore, the present invention provides an inertial dust collector, which improves and optimizes the original device. The inertial dust collector can not only reduce the secondary dust, but also reduce the resistance in the process of gas flow, and also improve the dust removal efficiency to a certain extent. Moreover, the reduction of the inlet wind pressure directly reduces the power of the fan, achieving the effect of saving energy.

发明内容Contents of the invention

本发明为一种双灰斗惯性除尘器,本发明要解决的问题是减少除尘过程中易出现的二次扬尘现象,减少了气体流动过程中的阻力,在一定程度上提高了除尘效率。The invention is an inertial dust collector with double ash hoppers. The problem to be solved by the invention is to reduce the secondary dust phenomenon that is easy to occur in the dust removal process, reduce the resistance in the gas flow process, and improve the dust removal efficiency to a certain extent.

本发明所采用的技术方案:The technical scheme adopted in the present invention:

提供一种双灰斗惯性除尘器,包括含尘气体入口,净化气体出口,灰斗,拐角,挡板,压力平衡孔等。Provided is an inertial dust collector with double ash hoppers, including a dusty gas inlet, a purified gas outlet, ash hoppers, corners, baffles, pressure balance holes, etc.

采用上述结构后,通过设置多个截面突变和倾斜挡板来使含尘气体通过惯性力和离心力的作用使灰尘落入两个灰斗中,净化后气体通过净化气体出口排出。After adopting the above structure, the dust-laden gas will fall into the two ash hoppers through the action of inertial force and centrifugal force by setting multiple cross-sectional mutations and inclined baffles, and the purified gas will be discharged through the purified gas outlet.

在入口处采用喷管加速来提高含尘气体的进口流速,使速度达到一个合适的数值,气体经加速后垂直射入除尘器碰撞到第一个阻碍——倾斜挡板。第一次经过碰撞摩擦减速,较大的颗粒粒子被倾斜挡板约束运动方向,进而被减速进入灰斗1,较小的灰尘颗粒随气流转弯进一步减速,由于离心力进入灰斗2。除尘器设置多个截面突变和倾斜挡板,主要是为了增大摩擦,整体上减小流体流速。除尘器总体体积较现有的惯性除尘器大大缩小,可以更加灵活的适应一些狭窄空间。如在大空间使用可并联多个该除尘器。如除尘器正视图剖图所示,灰斗2左侧设置有压力平衡孔,其作用为平衡灰斗2和外部环境的大气压,改善灰斗2内的流体状态,便于灰尘更好地除去,为防止灰尘堵塞压力平衡孔,故把其位置设置在灰斗2靠上部位置,为防止灰尘从压力平衡孔跑出,要在孔外设置一层细密的过滤装置。At the inlet, nozzle acceleration is used to increase the inlet flow velocity of the dusty gas, so that the velocity reaches a suitable value. After acceleration, the gas is vertically injected into the dust collector and collides with the first obstacle - the inclined baffle. After the first deceleration by collision and friction, the larger particles are restrained by the inclined baffle in the direction of movement, and then decelerated into the ash hopper 1, and the smaller dust particles are further decelerated with the turning of the airflow, and enter the ash hopper 2 due to centrifugal force. The dust collector is equipped with multiple cross-sectional mutations and inclined baffles, mainly to increase friction and reduce the fluid flow rate as a whole. Compared with the existing inertial dust collector, the overall volume of the dust collector is greatly reduced, and it can be more flexibly adapted to some narrow spaces. If it is used in a large space, multiple dust collectors can be connected in parallel. As shown in the sectional view of the front view of the dust collector, there is a pressure balance hole on the left side of the ash hopper 2, which functions to balance the atmospheric pressure between the ash hopper 2 and the external environment, improve the fluid state in the ash hopper 2, and facilitate better removal of dust. In order to prevent dust from clogging the pressure balance hole, its position is arranged on the upper part of the ash hopper 2. In order to prevent dust from running out of the pressure balance hole, a fine filter device should be arranged outside the hole.

附图说明Description of drawings

图1是本发明双灰斗惯性除尘器的正视图剖视图。Fig. 1 is a front view sectional view of the double ash hopper inertial dust collector of the present invention.

图1中1为含尘气体入口,2为拐角,3为挡板2,4为灰斗1,5为挡板3,6为挡板4,7为压力平衡孔,8为灰斗2,9为挡板5,10为净化气体出口,11为挡板1。In Figure 1, 1 is the dusty gas inlet, 2 is the corner, 3 is the baffle 2, 4 is the ash hopper 1, 5 is the baffle 3, 6 is the baffle 4, 7 is the pressure balance hole, 8 is the ash hopper 2, 9 is the baffle plate 5, 10 is the outlet of the purified gas, and 11 is the baffle plate 1.

具体实施措施Specific implementation measures

含尘气体在入口处通过喷管加速来使流速达到一个合适的数值,加速后的气体射入倾斜挡板1,首次经过碰撞摩擦减速,较大的颗粒粒子被倾斜挡板约束运动方向,进而被减速进入灰斗1的方向,再通过挡板2挡板3的摩擦减速的作用落入灰斗1,较小的灰尘颗粒随气流转弯进一步减速,由于离心力进入灰斗2方向,再通过挡板4挡板5的摩擦减速的作用落入灰斗2。而除尘后被净化的气体则从净化气体出口排出。除尘器总体体积较现有的惯性除尘器大大缩小,可以更加灵活的适应一些狭窄空间。如在大空间使用可并联多个该除尘器。如除尘器正视图剖图所示,灰斗2左侧设置有压力平衡孔,其作用为平衡灰斗2和外部环境的大气压,改善灰斗2内的流体状态,便于灰尘更好地除去,为防止灰尘堵塞压力平衡孔,故把其位置设置在灰斗2靠上部位置,为防止灰尘从压力平衡孔跑出,要在孔外设置一层细密的过滤装置。The dust-laden gas is accelerated through the nozzle at the entrance to make the flow rate reach a suitable value. The accelerated gas is injected into the inclined baffle 1, and is decelerated by collision and friction for the first time. The larger particles are restrained by the inclined baffle in the direction of movement, and then It is decelerated into the direction of the ash hopper 1, and then falls into the ash hopper 1 through the frictional deceleration of the baffle 2 and the baffle 3. The smaller dust particles are further decelerated with the turning of the airflow, and enter the direction of the ash hopper 2 due to centrifugal force, and then pass through the baffle. The effect of the frictional deceleration of the plate 4 baffle 5 falls into the ash hopper 2 . The purified gas after dust removal is discharged from the purified gas outlet. Compared with the existing inertial dust collector, the overall volume of the dust collector is greatly reduced, and it can be more flexibly adapted to some narrow spaces. If it is used in a large space, multiple dust collectors can be connected in parallel. As shown in the cutaway front view of the dust collector, there is a pressure balance hole on the left side of the ash hopper 2, which functions to balance the atmospheric pressure between the ash hopper 2 and the external environment, improve the fluid state in the ash hopper 2, and facilitate better dust removal. In order to prevent dust from clogging the pressure balance hole, its position is arranged on the upper part of the ash hopper 2. In order to prevent dust from running out of the pressure balance hole, a fine filter device should be arranged outside the hole.

Claims (3)

1. a kind of double ash bucket inertial dust separators, which is characterized in that including dusty gas entrance, sloping baffle 1, turning and baffle 2 It is connected, baffle 2, baffle 3 are connected with ash bucket 1, and baffle 3 is connected with baffle 4, and baffle 4, baffle 5 are connected with ash bucket 2,2 left side of ash bucket It is provided with pressure compensation opening.
2. a kind of double ash bucket inertial dust separators according to claim 1, it is characterised in that dusty gas entrance uses rectangle gradually Contracting jet pipe accelerates to improve dusty gas inlet velocity, so that speed is reached a suitable numerical value, is vertically penetrated after gas is accelerated Enter deduster and collide first obstruction --- sloping baffle.
3. a kind of double ash bucket inertial dust separators according to claim 1, it is characterised in that if deduster front view cuts open shown in figure, The left side of ash bucket 2 is provided with pressure compensation opening, position setting ash bucket 2 by the upper position, one layer of fine and closely woven mistake is set outside hole Filter device.
CN201810553610.2A 2018-06-01 2018-06-01 A kind of double ash bucket inertial dust separators Pending CN108392903A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810553610.2A CN108392903A (en) 2018-06-01 2018-06-01 A kind of double ash bucket inertial dust separators

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810553610.2A CN108392903A (en) 2018-06-01 2018-06-01 A kind of double ash bucket inertial dust separators

Publications (1)

Publication Number Publication Date
CN108392903A true CN108392903A (en) 2018-08-14

Family

ID=63102692

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810553610.2A Pending CN108392903A (en) 2018-06-01 2018-06-01 A kind of double ash bucket inertial dust separators

Country Status (1)

Country Link
CN (1) CN108392903A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN119761267A (en) * 2025-03-06 2025-04-04 包头市宜茂诚安物流有限责任公司 An intelligent control method and system for dry dust removal vehicle based on numerical simulation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201020413Y (en) * 2007-03-06 2008-02-13 张圣伟 Cyclone separator
CN205683775U (en) * 2016-03-24 2016-11-16 贵州大学 Gravitational settling and multistage impact type inertial dust separator

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201020413Y (en) * 2007-03-06 2008-02-13 张圣伟 Cyclone separator
CN205683775U (en) * 2016-03-24 2016-11-16 贵州大学 Gravitational settling and multistage impact type inertial dust separator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN119761267A (en) * 2025-03-06 2025-04-04 包头市宜茂诚安物流有限责任公司 An intelligent control method and system for dry dust removal vehicle based on numerical simulation
CN119761267B (en) * 2025-03-06 2025-07-04 包头市宜茂诚安物流有限责任公司 Intelligent control method and system for dry dust removal vehicle based on numerical simulation

Similar Documents

Publication Publication Date Title
CN107213739B (en) Novel high-efficient combined type wet dust collector in colliery
CN111467884A (en) Front dust removal and collection system of cloth bag type air dust collector
CN110585806A (en) Boundary separation dust collecting equipment
CN212700960U (en) Air filter with dust-proof air inlet
CN108392903A (en) A kind of double ash bucket inertial dust separators
CN112057957A (en) Air inlet duct with sand-proof dust-removing and silencing structure
CN204478606U (en) Oil separator and air conditioning device
CN208466198U (en) A kind of introducing-type cyclone separator
CN203469669U (en) High-efficiency and wear-resistant inertial dust collector
CN207445851U (en) A kind of New Coal Mine efficient composite wet scrubber
CN207203760U (en) A kind of high negative pressure deduster
CN206549853U (en) A kind of cyclone separator
CN110479506A (en) A kind of cyclone dust collectors and its dust removal method
CN212491947U (en) Air inlet duct with sand-proof dust-removing and silencing structure
CN112973368B (en) Dust-containing airflow rectifying and stabilizing device
CN115582260A (en) An automatic powder return device and a powder spreader including the same
CN104436949A (en) Device for collecting and filtering steam of metal dust
CN204380474U (en) Automation dust arrester
CN202942779U (en) Airflow short circuit preventing energy-saving efficient deduster
CN102600997A (en) High-efficiency dust collection cyclone separator group
CN112843974B (en) Coalescence device for promoting agglomeration of particles
CN207247929U (en) Solid-gas separation flue
JPS6341077Y2 (en)
CN204469921U (en) A kind of Y shape entrance vertical cut formula cyclone separator
CN107648952A (en) A kind of venturi injection tube for deduster

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
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180814