CN118698269A - An environmentally friendly dust removal and exhaust method - Google Patents
An environmentally friendly dust removal and exhaust method Download PDFInfo
- Publication number
- CN118698269A CN118698269A CN202410975175.8A CN202410975175A CN118698269A CN 118698269 A CN118698269 A CN 118698269A CN 202410975175 A CN202410975175 A CN 202410975175A CN 118698269 A CN118698269 A CN 118698269A
- Authority
- CN
- China
- Prior art keywords
- dust
- exhaust
- gas
- air
- bag
- 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
Links
- 239000000428 dust Substances 0.000 title claims abstract description 169
- 238000000034 method Methods 0.000 title claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 124
- 238000000926 separation method Methods 0.000 claims abstract description 69
- 238000001914 filtration Methods 0.000 claims abstract description 39
- 239000002912 waste gas Substances 0.000 claims abstract description 22
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 21
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 21
- 230000005540 biological transmission Effects 0.000 claims abstract description 20
- 238000002955 isolation Methods 0.000 claims abstract description 17
- 238000005266 casting Methods 0.000 claims abstract description 13
- 238000004062 sedimentation Methods 0.000 claims description 63
- 238000012546 transfer Methods 0.000 claims description 24
- 239000011362 coarse particle Substances 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 14
- 238000007599 discharging Methods 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 8
- 230000007613 environmental effect Effects 0.000 claims description 6
- 230000000694 effects Effects 0.000 abstract description 8
- 238000000746 purification Methods 0.000 abstract description 6
- 239000002956 ash Substances 0.000 description 18
- 239000002245 particle Substances 0.000 description 12
- 239000002893 slag Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000000463 material Substances 0.000 description 7
- 238000010408 sweeping Methods 0.000 description 7
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 6
- 239000004568 cement Substances 0.000 description 6
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 239000000839 emulsion Substances 0.000 description 6
- 238000003723 Smelting Methods 0.000 description 5
- 230000009471 action Effects 0.000 description 5
- 239000003638 chemical reducing agent Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- 238000006073 displacement reaction Methods 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 238000003780 insertion Methods 0.000 description 4
- 230000037431 insertion Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000002923 metal particle Substances 0.000 description 4
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2r)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 229920005646 polycarboxylate Polymers 0.000 description 2
- 229920001296 polysiloxane Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
-
- 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
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Treating Waste Gases (AREA)
Abstract
本申请涉及废气净化处理技术领域,尤其是涉及一种环保除尘排气方法,包括:S1:通过进气组件使铝棒熔铸废气进入传气管道;S2:通过传气管道使废气进入沉降件进行初步沉降,初步沉降后进入分离过滤箱的分离腔;S3:废气进入分离腔后进行二次沉降,然后进入过滤腔进行过滤;S4:通过滤气组件对进入过滤腔的气体进行过滤,气体过滤后进入隔离室,然后将隔离室的气体转移到排气囱进行排出。本申请具有减少铝熔铸排气污染的效果。
The present application relates to the technical field of waste gas purification and treatment, and in particular to an environmentally friendly dust removal and exhaust method, comprising: S1: allowing the waste gas from aluminum rod casting to enter the air transmission pipeline through the air intake assembly; S2: allowing the waste gas to enter the settling piece through the air transmission pipeline for preliminary settling, and then enter the separation chamber of the separation filter box after preliminary settling; S3: after the waste gas enters the separation chamber, it undergoes secondary settling, and then enters the filter chamber for filtration; S4: filtering the gas entering the filter chamber through the air filter assembly, and the gas enters the isolation chamber after filtration, and then the gas in the isolation chamber is transferred to the exhaust chimney for discharge. The present application has the effect of reducing the pollution of aluminum casting exhaust.
Description
技术领域Technical Field
本申请涉及废气净化处理技术领域,尤其是涉及一种环保除尘排气方法。The present application relates to the technical field of waste gas purification and treatment, and in particular to an environmentally friendly dust removal and exhaust method.
背景技术Background Art
目前,铝棒的熔铸包括熔化、提纯、除杂、除气、除渣与铸造过程,在其过程中,需要使用高温熔铸设备将铝材熔化,并将铝与其它杂质相互分离,然后提取出铝液进行进一步加工提纯。At present, the smelting and casting of aluminum rods includes melting, purification, impurity removal, degassing, slag removal and casting processes. During the process, high-temperature melting and casting equipment is needed to melt the aluminum material, separate the aluminum from other impurities, and then extract the aluminum liquid for further processing and purification.
而在熔化铝材的过程中,通常会产生大量含金属碎屑与粉尘的废气,若直接排放,将对环境造成严重的污染,现有的除尘方法中,仅将废气引入除尘器中进行一道过滤工序,然后直接排放,无法保证废气得到足够的净化后进行过滤,容易对环境造成较大的污染,且废气中的金属碎屑与粉尘有可能对过滤的袋子进行剐蹭或腐蚀,从而对滤尘袋子造成破坏,使废气还未完成充足的过滤就排放,从而对环境造成污染。In the process of melting aluminum, a large amount of waste gas containing metal debris and dust is usually generated. If it is discharged directly, it will cause serious pollution to the environment. In the existing dust removal method, the waste gas is only introduced into the dust collector for a filtering process and then discharged directly. It cannot ensure that the waste gas is sufficiently purified before filtering, which is easy to cause greater pollution to the environment. The metal debris and dust in the waste gas may scratch or corrode the filter bag, thereby damaging the dust filter bag, causing the waste gas to be discharged before sufficient filtration is completed, thereby polluting the environment.
发明内容Summary of the invention
为了减少铝熔铸的排气污染,本申请提供一种环保除尘排气方法。In order to reduce exhaust pollution from aluminum smelting and casting, the present application provides an environmentally friendly dust removal and exhaust method.
本申请提供的一种环保除尘排气方法,采用如下的技术方案:The present application provides an environmentally friendly dust removal and exhaust method, which adopts the following technical solutions:
一种环保除尘排气方法,包括以下步骤:S1:通过进气组件使铝棒熔铸废气进入传气管道;S2:通过传气管道使废气进入沉降件进行初步沉降,初步沉降后进入分离过滤箱的分离腔;S3:废气进入分离腔后进行二次沉降,然后进入过滤腔进行过滤;S4:通过滤气组件对进入过滤腔的废气进行过滤,气体过滤后进入隔离室,然后将隔离室的气体转移到排气囱进行排出。An environmentally friendly dust removal and exhaust method comprises the following steps: S1: allowing aluminum rod casting waste gas to enter an air transmission pipeline through an air intake assembly; S2: allowing the waste gas to enter a sedimentation piece through the air transmission pipeline for preliminary sedimentation, and then enter a separation chamber of a separation filter box after preliminary sedimentation; S3: after the waste gas enters the separation chamber, it undergoes secondary sedimentation, and then enters a filter chamber for filtration; S4: filtering the waste gas entering the filter chamber through an air filter assembly, and the gas enters an isolation chamber after filtration, and then the gas in the isolation chamber is transferred to an exhaust chimney for discharge.
通过采用上述技术方案,通过初步沉降使废气中的粗颗粒碎屑与一部分粉尘先脱离出废气,然后进入分离腔通过二次沉降使废气中的粗颗粒粉尘与剩余的碎屑再度脱离废气,剩余的细颗粒粉尘跟随废气进入过滤腔再进行过滤,使废气与碎屑粉尘得到充分的分离,减少碎屑与粉尘对滤气组件的剐蹭或腐蚀,可使废气中的绝大部分粉尘留在沉降件、分离腔与过滤腔中,从而减少过滤后排放的气体对环境的污染。By adopting the above technical scheme, the coarse particles and debris and a part of the dust in the exhaust gas are separated from the exhaust gas through preliminary sedimentation, and then enter the separation chamber for secondary sedimentation to separate the coarse particles and the remaining debris in the exhaust gas from the exhaust gas again, and the remaining fine particles follow the exhaust gas into the filter chamber for further filtration, so that the exhaust gas and the debris dust are fully separated, and the scratches or corrosion of the filter components by the debris and dust are reduced, and most of the dust in the exhaust gas can be retained in the sedimentation parts, the separation chamber and the filter chamber, thereby reducing the pollution of the gas discharged after filtration to the environment.
可选的,步骤S2中,废气从传气管道进入沉降件后,通过影响废气的流速,使废气进行初步沉降。Optionally, in step S2, after the exhaust gas enters the settling member from the gas transmission pipe, the exhaust gas is initially settled by affecting the flow rate of the exhaust gas.
通过采用上述技术方案,使碎屑与粉尘在重力作用下发生沉降,影响废气的流速使废气的流速变慢,从而可使碎屑与粉尘脱离得到更充分的沉降。By adopting the above technical solution, the debris and dust are allowed to settle under the action of gravity, which affects the flow rate of the exhaust gas and slows it down, so that the debris and dust can be separated and settled more fully.
可选的,所述沉降件包括沉降管,所述沉降管与传气管道相连通,所述沉降管的侧壁开设有连通于分离腔的进风口,所述沉降管中的废气可通过进风口进入分离腔,所述沉降管的底部呈倾斜设置。Optionally, the sedimentation member includes a sedimentation pipe, which is connected to the air transfer pipe. The side wall of the sedimentation pipe is provided with an air inlet connected to the separation chamber. The exhaust gas in the sedimentation pipe can enter the separation chamber through the air inlet. The bottom of the sedimentation pipe is inclined.
通过采用上述技术方案,沉降的粗颗粒碎屑可通过通风口与倾斜面滑落到入分离腔,从而便于收集。By adopting the above technical solution, the settled coarse particle debris can slide into the separation chamber through the ventilation opening and the inclined surface, thereby facilitating collection.
可选的,所述沉降管的内径大小沿远离传气管道的方向呈逐渐减小,所述进风口沿远离传气管道的方向排列。Optionally, the inner diameter of the settling pipe gradually decreases in a direction away from the air transfer pipe, and the air inlets are arranged in a direction away from the air transfer pipe.
通过采用上述技术方案,可增加废气进入沉降管后的阻力,进一步减慢废气的流速。By adopting the above technical solution, the resistance of the exhaust gas after entering the settling pipe can be increased, and the flow rate of the exhaust gas can be further slowed down.
可选的,步骤S3中,废气进入分离腔后,二次沉降的粗颗粒粉尘掉落在分离腔的底部,通过设置在分离过滤箱底部的收集组件进行收集。Optionally, in step S3, after the exhaust gas enters the separation chamber, the coarse dust particles that are secondary settled fall to the bottom of the separation chamber and are collected by a collection assembly disposed at the bottom of the separation filter box.
通过采用上述技术方案,使用收集组件对粉尘与碎屑进行收集可便于回收集中处理。By adopting the above technical solution, dust and debris can be collected using a collection component to facilitate recycling and centralized treatment.
可选的,所述收集组件包括位于分离腔下方的收集转移箱,所述收集转移箱的出料端设有集灰袋,在进行步骤S2-S4的过程中,当集灰袋集满粉尘时,通过设置在收集转移箱上的换装组件对集灰袋进行更换。Optionally, the collecting assembly includes a collecting and transferring box located below the separation chamber, and a dust collecting bag is provided at the discharge end of the collecting and transferring box. During steps S2-S4, when the dust collecting bag is full of dust, the dust collecting bag is replaced by a replacement assembly arranged on the collecting and transferring box.
通过采用上述技术方案,集灰袋满载时,通过换装组件进行更换,从更换其它集灰袋进行收集,实现不间断收集粉尘。By adopting the above technical solution, when the dust collecting bag is fully loaded, it can be replaced by replacing the assembly, and then other dust collecting bags can be replaced to collect dust, thereby realizing uninterrupted dust collection.
可选的,所述换装组件包括固定架与横移座,所述固定架与收集转移箱相连接,所述横移座与固定架滑移连接,所述横移座上可拆卸式设置有拆装架,所述拆装架的数量不低于两件,所述集灰袋与拆装架相连接。Optionally, the replacement assembly includes a fixed frame and a transverse seat, the fixed frame is connected to the collection and transfer box, the transverse seat is slidably connected to the fixed frame, the transverse seat is detachably provided with a disassembly frame, the number of the disassembly frames is not less than two, and the dust collection bag is connected to the disassembly frame.
通过采用上述技术方案,使用一个集灰袋在进行收集工作时,另一个集灰袋备用,更换时滑移横移座,可替代原先收集工作的集灰袋进行收集,并可以拆出满载状态的集灰袋更换,实现不间断集灰。By adopting the above technical solution, one ash bag is used for collection while the other ash bag is kept as a standby. When replacing, the sliding transverse seat can replace the original ash bag for collection, and the fully loaded ash bag can be removed and replaced to achieve uninterrupted ash collection.
可选的,步骤S4中,气体通过滤气组件过滤后进入出风管,排风驱动件将出风管中的气体抽到排气囱中。Optionally, in step S4, the gas enters the air outlet pipe after being filtered by the air filter assembly, and the exhaust drive element draws the gas in the air outlet pipe into the exhaust chimney.
通过采用上述技术方案,气体抽到排气囱中排放可提高排放高度,降低对周围地面环境的影响,排放到较高的高度后,大气的湍流和扩散作用,使排放的气体可以更快地被稀释。By adopting the above technical solution, the gas can be discharged into the exhaust chimney to increase the discharge height and reduce the impact on the surrounding ground environment. After being discharged to a higher altitude, the turbulence and diffusion of the atmosphere can dilute the discharged gas more quickly.
可选的,在步骤S4后加入步骤S5:启动脱尘驱动件,对除尘室内的滤气组件间歇式喷气。Optionally, step S5 is added after step S4: starting the dust removal drive component to intermittently spray air to the air filter assembly in the dust removal chamber.
通过采用上述技术方案,对滤气组件喷气可将附着在滤气组件上的细颗粒粉尘吹落,从而有助于滤气组件保持预期的可过滤气体量。By adopting the above technical solution, the fine dust particles attached to the air filter component can be blown off by jetting air to the air filter component, thereby helping the air filter component to maintain the expected filterable gas volume.
可选的,所述滤气组件包括滤尘袋,所述分离过滤箱内设有隔板,所述隔板开设有通气孔,所述滤尘袋安装在通气孔处,所述滤气组件还包括外笼架,所述外笼架与隔板相连接,所述外笼架罩设在滤尘袋的周侧。Optionally, the air filter assembly includes a dust filter bag, a partition is provided in the separation filter box, the partition is provided with an air vent, the dust filter bag is installed at the air vent, and the air filter assembly also includes an outer cage frame, the outer cage frame is connected to the partition, and the outer cage frame cover is provided on the surrounding side of the dust filter bag.
通过采用上述技术方案,对滤尘袋喷气除尘时,外笼架可对滤尘袋进行外部支撑与限位,提高滤尘袋稳定性,减少使用大风力时滤尘袋过度膨胀的情况。By adopting the above technical solution, when the dust filter bag is jetted for dust removal, the outer cage frame can provide external support and limit the dust filter bag, thereby improving the stability of the dust filter bag and reducing the excessive expansion of the dust filter bag when using strong wind force.
综上所述,本申请包括以下至少一种有益技术效果:In summary, the present application includes at least one of the following beneficial technical effects:
1.通过初步沉降使废气中的粗颗粒碎屑与一部分粉尘先脱离出废气,然后进入分离腔通过二次沉降使废气中的粗颗粒粉尘与剩余的碎屑再度脱离废气,剩余的细颗粒粉尘跟随废气进入过滤腔再进行过滤,使废气与碎屑粉尘得到充分的分离,此状态下可使废气中的绝大部分粉尘留在沉降件、分离腔与过滤腔中,从而减少过滤后排放的气体对环境的污染;1. Through the initial sedimentation, the coarse particles and debris in the exhaust gas and a part of the dust are separated from the exhaust gas first, and then enter the separation chamber for secondary sedimentation to separate the coarse particles and the remaining debris in the exhaust gas from the exhaust gas again. The remaining fine particles follow the exhaust gas into the filter chamber for further filtration, so that the exhaust gas and the debris dust are fully separated. In this state, most of the dust in the exhaust gas can be left in the sedimentation piece, the separation chamber and the filter chamber, thereby reducing the pollution of the gas discharged after filtration to the environment;
2.使碎屑与粉尘在重力作用下发生沉降,影响废气的流速使废气的流速变慢,从而可使碎屑与粉尘脱离得到更充分的沉降;2. Make the debris and dust settle under the action of gravity, affect the flow rate of the exhaust gas and slow down the flow rate of the exhaust gas, so that the debris and dust can be separated and settled more fully;
3.使用一个集灰袋在进行收集工作时,另一个集灰袋备用,更换时滑移横移座,可替代原先收集工作的集灰袋进行收集,并可以拆出满载状态的集灰袋更换,实现不间断集灰。3. When one ash bag is used for collection, the other ash bag is kept as a standby. When replacing, the sliding transverse seat can replace the original ash bag for collection, and the fully loaded ash bag can be removed and replaced to achieve uninterrupted ash collection.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1是本申请实施例中除尘排气装置的外部结构示意图。FIG. 1 is a schematic diagram of the external structure of a dust removal and exhaust device in an embodiment of the present application.
图2是本申请实施例中除尘排气装置的另一视角示意图。FIG. 2 is a schematic diagram of the dust removal and exhaust device in the embodiment of the present application from another perspective.
图3是本申请实施例中除尘排气装置的内部结构示意图。FIG. 3 is a schematic diagram of the internal structure of the dust removal and exhaust device in an embodiment of the present application.
图4是本申请实施例中沉降管的内部结构示意图。FIG. 4 is a schematic diagram of the internal structure of a settling tube in an embodiment of the present application.
图5是本申请实施例中除尘排气装置的另一视角内部结构图。FIG. 5 is a diagram showing the internal structure of the dust removal and exhaust device from another perspective in an embodiment of the present application.
图6是本申请实施例中固定架、横移座与拆装架的局部剖视图。FIG6 is a partial cross-sectional view of the fixed frame, the transverse seat and the disassembly frame in the embodiment of the present application.
图7是本申请实施例中驱动杆与延伸杆的连接示意图。FIG. 7 is a schematic diagram of the connection between the driving rod and the extension rod in an embodiment of the present application.
图8是本申请实施例中内笼架、滤尘袋与外笼架的结构剖视图。FIG8 is a cross-sectional view of the structure of the inner cage frame, the dust filter bag and the outer cage frame in the embodiment of the present application.
附图标记说明:Description of reference numerals:
1、进气组件;11、传气管道;2、沉降管;21、进风口;3、分离过滤箱;31、分离腔;32、过滤腔;33、隔离室;34、隔板;341、滤尘袋;342、外笼架;343、内笼架;35、出风管;351、排风驱动件;36、转动环;361、延伸杆;37、转动驱动件;38、驱动杆;39、脱尘驱动件;4、排气囱;5、收集转移箱;51、收料孔;52、出料电机;53、转动杆;54、螺旋桨带;55、集灰袋;551、连接环;56、固定座;561、插孔;57、空孔;571、扫架;572、扫毛;6、固定架;61、横移座;611、阶梯通槽;62、横移驱动件;63、拆装架;631、插块;632、插环;64、起降驱动件;65、起降座;651、环形槽;652、压力传感器。1. Intake assembly; 11. Air transmission duct; 2. Settling pipe; 21. Air inlet; 3. Separation filter box; 31. Separation chamber; 32. Filter chamber; 33. Isolation chamber; 34. Partition; 341. Dust filter bag; 342. Outer cage; 343. Inner cage; 35. Air outlet pipe; 351. Exhaust drive; 36. Rotating ring; 361. Extension rod; 37. Rotating drive; 38. Drive rod; 39. Dust removal drive; 4. Exhaust chimney; 5. Collection transfer box; 51. Material receiving hole; 52, material discharging motor; 53, rotating rod; 54, propeller belt; 55, dust collecting bag; 551, connecting ring; 56, fixed seat; 561, plug hole; 57, empty hole; 571, sweeping frame; 572, sweeping hair; 6, fixed frame; 61, transverse seat; 611, stepped through groove; 62, transverse driving part; 63, disassembly and assembly frame; 631, plug block; 632, plug ring; 64, lifting and landing driving part; 65, lifting and landing seat; 651, annular groove; 652, pressure sensor.
具体实施方式DETAILED DESCRIPTION
以下结合附图1-8对本申请作进一步详细说明。The present application is further described in detail below in conjunction with Figures 1-8.
本申请实施例公开一种环保除尘排气方法。The embodiment of the present application discloses an environmentally friendly dust removal and exhaust method.
参照图1与图2,一种环保除尘排气方法,包括以下步骤:1 and 2, an environmentally friendly dust removal and exhaust method includes the following steps:
S1:采用除尘排气装置,令除尘排气装置与铝棒熔铸设备相靠近,参照图1与图3,除尘排气装置包括进气组件1、传气管道11、沉降件、分离过滤箱3、滤气组件与排气囱4,分离过滤箱3通过支架安装在地面,分离过滤箱3的内部开设有分离腔31、过滤腔32与隔离室33,令进气组件1位于铝棒熔铸设备的排气口上方,通过进气组件1使铝棒熔铸废气进入传气管道11,排气囱4设置在分离过滤箱3的外侧;S1: A dust removal exhaust device is used, and the dust removal exhaust device is placed close to the aluminum rod smelting and casting equipment. Referring to Figures 1 and 3, the dust removal and exhaust device includes an air intake component 1, an air transmission pipeline 11, a settling piece, a separation filter box 3, an air filter component and an exhaust chimney 4. The separation filter box 3 is installed on the ground through a bracket. A separation chamber 31, a filter chamber 32 and an isolation chamber 33 are provided inside the separation filter box 3. The air intake component 1 is located above the exhaust port of the aluminum rod smelting and casting equipment, and the aluminum rod smelting and casting waste gas enters the air transmission pipeline 11 through the air intake component 1. The exhaust chimney 4 is arranged on the outside of the separation filter box 3;
S2:通过传气管道11使废气进入沉降件中,使废气在沉降件内进行初步沉降,使部分大颗粒物与气体相脱离,脱离的大颗粒物掉落到沉降件的底部,废气在初步沉降后进入分离腔31;S2: The exhaust gas enters the settling piece through the gas transmission pipe 11, and the exhaust gas is initially settled in the settling piece, so that some large particles are separated from the gas phase, and the separated large particles fall to the bottom of the settling piece. After the initial settling, the exhaust gas enters the separation chamber 31;
S3:废气进入分离腔31后进行二次沉降,分离腔31中粗颗粒粉尘与气体相互脱离,脱离的粗颗粒粉尘掉落在分离腔31的底部,废气在二次脱离后进入过滤腔32进行过滤;S3: After the exhaust gas enters the separation chamber 31, it undergoes secondary sedimentation. The coarse dust particles in the separation chamber 31 are separated from the gas. The separated coarse dust particles fall to the bottom of the separation chamber 31. After the secondary separation, the exhaust gas enters the filter chamber 32 for filtration.
S4:二次脱离后的废气进入滤气组件,通过滤气组件对进入过滤腔32的废气进行过滤,气体过滤后进入隔离室33,然后将隔离室33的气体转移到排气囱4进行排出。S4: The waste gas after the secondary separation enters the gas filter assembly, and the waste gas entering the filter chamber 32 is filtered by the gas filter assembly. After the gas is filtered, it enters the isolation chamber 33, and then the gas in the isolation chamber 33 is transferred to the exhaust chimney 4 for discharge.
通过两次沉降依次使废气中的金属颗粒以及粉尘等粗颗粒物从废气中分离,然后通过滤气组件将废气中剩余的细小颗粒粉尘与气体相互分离,从而完成气体的过滤净化,通过隔离室33与过滤腔32将过滤后与过滤前的空气相分隔,将过滤干净的气体排出,减少排出气体中携带的金属颗粒与粉尘,沉降与过滤过程中,废气与碎屑粉尘得到充分的分离,减少碎屑与粉尘对滤气组件的剐蹭或腐蚀,减少过滤后排放的气体对环境的污染,从而达到环保排气的效果。Through two sedimentation steps, metal particles and coarse particles such as dust in the exhaust gas are separated from the exhaust gas in turn, and then the fine particles and dust remaining in the exhaust gas are separated from the gas through the air filter component, thereby completing the gas filtering and purification. The air after filtration is separated from the air before filtration through the isolation chamber 33 and the filter cavity 32, and the filtered gas is discharged to reduce the metal particles and dust carried in the exhaust gas. During the sedimentation and filtration process, the exhaust gas and debris dust are fully separated, reducing the scratches or corrosion of the filter component by debris and dust, and reducing the pollution of the gas discharged after filtration to the environment, thereby achieving the effect of environmentally friendly exhaust.
参照图2与图4,传气管道11的一端与沉降件相连接,进气组件1由进气驱动件与进气罩组成,进气罩安装在传气管道11远离沉降件的一端,进气驱动件为抽风机,进气驱动件安装在进气罩的内部,进气罩位于铝棒熔铸设备的排气口上方,工作时,铝棒熔铸设备产生废气,进气驱动件将废气通过进气罩抽入传气管道11,并在传气管道11内形成气流,使废气流向沉降件,传气管道11由金属制成,在传输废气的过程中,可将废气的热量向外散发,从而起到降温效果。Referring to Figures 2 and 4, one end of the air transfer pipe 11 is connected to the settlement piece, and the air intake assembly 1 is composed of an air intake drive and an air intake hood. The air intake hood is installed at one end of the air transfer pipe 11 away from the settlement piece. The air intake drive is an exhaust fan, and the air intake drive is installed inside the air intake hood. The air intake hood is located above the exhaust port of the aluminum rod casting equipment. During operation, the aluminum rod casting equipment generates exhaust gas, and the air intake drive draws the exhaust gas into the air transfer pipe 11 through the air intake hood, and forms an airflow in the air transfer pipe 11, so that the exhaust gas flows to the settlement piece. The air transfer pipe 11 is made of metal. In the process of transmitting the exhaust gas, the heat of the exhaust gas can be dissipated outward, thereby achieving a cooling effect.
步骤S1中,废气进入传气管道11传输的过程中,废气中的一部分粗颗粒碎屑与传气管道11的内壁相接触碰撞,从而进行减速,在传输的过程中完成一部分碎屑与气体的分离,同时粗颗粒碎屑也被气流吹向沉降件。In step S1, during the transmission of the exhaust gas into the air transfer pipe 11, a portion of the coarse particles in the exhaust gas come into contact with and collide with the inner wall of the air transfer pipe 11, thereby decelerating the exhaust gas. During the transmission process, a portion of the particles are separated from the gas, and at the same time, the coarse particles are also blown toward the sedimentation piece by the airflow.
步骤S2中,废气从传气管道11进入沉降件后,废气中大颗粒的金属碎屑在重力的作用下自动沉降,通过对沉降件影响废气的流速,使废气的流速发生改变,从而令废气进行初步沉降,本实施例中,通过改变沉降件内部空间的大小来调节废气流速,由于沉降件的内空间大小发生变化,因此废气在进入沉降件之后会经历由快变慢的过程,从而延长废气在沉降件内的时间,使得废气与粗颗粒碎屑可进行更充分的沉降。In step S2, after the exhaust gas enters the sedimentation piece from the air transfer pipe 11, the large particles of metal debris in the exhaust gas automatically settle under the action of gravity, and the flow rate of the exhaust gas is affected by the sedimentation piece, so that the flow rate of the exhaust gas is changed, thereby causing the exhaust gas to undergo preliminary sedimentation. In this embodiment, the exhaust gas flow rate is adjusted by changing the size of the internal space of the sedimentation piece. Since the size of the internal space of the sedimentation piece changes, the exhaust gas will experience a process of changing from fast to slow after entering the sedimentation piece, thereby extending the time the exhaust gas stays in the sedimentation piece, so that the exhaust gas and the coarse particles can be more fully settled.
参照图2与图4,沉降件包括沉降管2,沉降管2沿水平方向延伸,沉降管2的其中一端与传气管道11相连通,沉降管2的另一端呈封闭设置,沉降管2靠近传气管道11一端的内径大小大于传气管道11的内径大小,沉降管2的侧壁固定在分离过滤箱3的侧壁,沉降管2与分离过滤箱3为一体式设置,沉降管2靠近分离过滤箱3的一侧开设有连通于分离腔31的进风口21,沉降管2中的废气可通过进风口21进入分离腔31,废气从传气管道11进入沉降管2后由于内径变化,使得气体流速下降,使粗颗粒碎屑在重力作用下,向下掉落在沉降管2的底部,从而实现初步沉降。2 and 4 , the sedimentation member includes a sedimentation pipe 2, which extends in a horizontal direction. One end of the sedimentation pipe 2 is connected to the air transmission pipe 11, and the other end of the sedimentation pipe 2 is closed. The inner diameter of the end of the sedimentation pipe 2 close to the air transmission pipe 11 is larger than the inner diameter of the air transmission pipe 11. The side wall of the sedimentation pipe 2 is fixed to the side wall of the separation filter box 3. The sedimentation pipe 2 and the separation filter box 3 are integrally arranged. An air inlet 21 connected to the separation chamber 31 is provided on the side of the sedimentation pipe 2 close to the separation filter box 3. The exhaust gas in the sedimentation pipe 2 can enter the separation chamber 31 through the air inlet 21. After the exhaust gas enters the sedimentation pipe 2 from the air transmission pipe 11, the gas flow rate decreases due to the change in the inner diameter, so that the coarse particles and debris fall downward to the bottom of the sedimentation pipe 2 under the action of gravity, thereby achieving initial sedimentation.
参照图4与图5,沉降管2的底部呈倾斜设置,沉降管2的底部向靠近分离过滤箱3的方向呈向下倾斜,进风口21与沉降管2的底部相靠近,进风口21的底壁倾斜方向与沉降管2底部的倾斜方向相一致,初步沉降的粗颗粒碎屑脱离废气后掉落在沉降管2的内底壁,可沿倾斜的底壁滑落掉入分离过滤箱3的分离腔31底部,便于进行收集。Referring to Figures 4 and 5, the bottom of the sedimentation pipe 2 is inclined, and the bottom of the sedimentation pipe 2 is inclined downward toward the separation filter box 3. The air inlet 21 is close to the bottom of the sedimentation pipe 2, and the inclination direction of the bottom wall of the air inlet 21 is consistent with the inclination direction of the bottom of the sedimentation pipe 2. The initially settled coarse particle debris separates from the exhaust gas and falls on the inner bottom wall of the sedimentation pipe 2, and can slide along the inclined bottom wall and fall into the bottom of the separation chamber 31 of the separation filter box 3, which is convenient for collection.
沉降管2的内径大小沿远离传气管道11的方向呈逐渐减小,进风口21沿沉降管2的延伸方向排列,废气从传气管道11进入沉降管2后,逐渐缩小的内径可增加废气与沉降管2内壁的接触概率,废气在沉降管2中的流道阻力增加,有助于降低废气流速,使得流速在靠近沉降管2末端时减慢,减弱废气携带颗粒物的能力,便于颗粒物沉降,且随着沉降管2内径的减小,废气流容易从湍流状态转变为层流状态,层流状态下的流速通常比湍流状态下的流速低,有助于粗颗粒碎屑的沉降,从而提高沉降效率。The inner diameter of the settling tube 2 gradually decreases in the direction away from the air transfer pipe 11, and the air inlet 21 is arranged along the extension direction of the settling tube 2. After the exhaust gas enters the settling tube 2 from the air transfer pipe 11, the gradually shrinking inner diameter can increase the contact probability between the exhaust gas and the inner wall of the settling tube 2. The flow resistance of the exhaust gas in the settling tube 2 increases, which helps to reduce the exhaust gas flow rate, so that the flow rate slows down when approaching the end of the settling tube 2, weakening the ability of the exhaust gas to carry particulate matter, and facilitating the sedimentation of particulate matter. As the inner diameter of the settling tube 2 decreases, the exhaust gas flow can easily change from a turbulent state to a laminar state. The flow rate in the laminar state is usually lower than the flow rate in the turbulent state, which helps to settle coarse particles and debris, thereby improving the sedimentation efficiency.
参照图3与图5,分离过滤箱3中,分离腔31与过滤腔32相连通,分离腔31位于过滤腔32的下方,分离腔31的容积大于沉降管2的内部容积,分离腔31竖直截面的面积大于沉降管2的内部竖直截面的面积,步骤S3中,废气从沉降管2进入分离腔31后,由于截面积增加,使废气的气流速度再次降低,使得一次沉降后废气接近漂浮状态,混杂在废气中的粗颗粒粉尘在重力作用下进行二次沉降,二次沉降的粗颗粒粉尘掉落在分离腔31的底部,通过设置在分离过滤箱3底部的收集组件对颗粒粉尘与碎屑进行收集。3 and 5, in the separation filter box 3, the separation chamber 31 is connected with the filter chamber 32, the separation chamber 31 is located below the filter chamber 32, the volume of the separation chamber 31 is larger than the internal volume of the sedimentation tube 2, the area of the vertical section of the separation chamber 31 is larger than the area of the internal vertical section of the sedimentation tube 2, in step S3, after the exhaust gas enters the separation chamber 31 from the sedimentation tube 2, the air flow velocity of the exhaust gas is reduced again due to the increase in the cross-sectional area, so that the exhaust gas is close to a floating state after the first sedimentation, and the coarse dust particles mixed in the exhaust gas are secondary settled under the action of gravity, and the secondary settled coarse dust particles fall to the bottom of the separation chamber 31, and the particle dust and debris are collected by the collecting assembly arranged at the bottom of the separation filter box 3.
参照图3与图5,收集组件包括位于分离腔31下方的收集转移箱5,收集转移箱5安装在分离过滤箱3的底侧,分离过滤箱3的底部呈斗状,具体地,分离过滤箱3的底部呈横截面逐渐缩小的倒梯形台状,分离过滤箱3的底侧开设有落料孔,落料孔与分离腔31相连通,收集转移箱5沿水平方向延伸,收集转移箱5的顶侧开设有与落料孔相对应的收料孔51,收集转移箱5的其中一端安装有出料电机52,收集转移箱5远离出料电机52的一端为出料端,收集转移箱5的内部转动连接有转动杆53,出料电机52的驱动端与转动杆53相连接,转动杆53上连接有螺旋桨带54,收集转移箱5的出料端底壁开设有连通于收集转移箱5内部的开口,收集转移箱5的出料端开口处设有集灰袋55,收集转移箱5的出料端底部设置有换装组件,集灰袋55安装在换装组件上,在进行步骤S2-S4的过程中,当集灰袋55集满粉尘与碎屑时,通过换装组件对集灰袋55进行更换。3 and 5 , the collecting assembly includes a collecting and transferring box 5 located below the separation chamber 31. The collecting and transferring box 5 is installed on the bottom side of the separation and filtering box 3. The bottom of the separation and filtering box 3 is in the shape of a bucket. Specifically, the bottom of the separation and filtering box 3 is in the shape of an inverted trapezoidal table with a gradually reduced cross-section. A material drop hole is provided on the bottom side of the separation and filtering box 3. The material drop hole is connected to the separation chamber 31. The collecting and transferring box 5 extends in the horizontal direction. A material receiving hole 51 corresponding to the material drop hole is provided on the top side of the collecting and transferring box 5. A discharging motor 52 is installed at one end of the collecting and transferring box 5. The collecting and transferring box 5 is away from the discharging motor 52. One end is the discharging end, and the interior of the collecting and transferring box 5 is rotatably connected with a rotating rod 53, the driving end of the discharging motor 52 is connected to the rotating rod 53, and the rotating rod 53 is connected with a propeller belt 54. The bottom wall of the discharging end of the collecting and transferring box 5 is provided with an opening connected to the interior of the collecting and transferring box 5, and a dust collecting bag 55 is provided at the opening of the discharging end of the collecting and transferring box 5. A replacement component is provided at the bottom of the discharging end of the collecting and transferring box 5, and the dust collecting bag 55 is installed on the replacement component. During the process of performing steps S2-S4, when the dust collecting bag 55 is full of dust and debris, the dust collecting bag 55 is replaced by the replacement component.
沉降过程中分离出的粉尘可掉落在分离过滤箱3的内底部,通过落料孔与收料孔51进入收集转移箱5中,令出料电机52驱使转动杆53转动,令转动杆53与螺旋桨带54将粉尘输向收集转移箱5的出料端,使收集的粉尘掉入集灰袋55中进行收集,当集灰袋55中装满粉尘时,可由工作人员通过换装组件将集灰袋55拆下进行更换。The dust separated during the sedimentation process can fall on the inner bottom of the separation filter box 3, and enter the collection transfer box 5 through the drop hole and the receiving hole 51, so that the discharge motor 52 drives the rotating rod 53 to rotate, and the rotating rod 53 and the propeller belt 54 transport the dust to the discharge end of the collection transfer box 5, so that the collected dust falls into the ash bag 55 for collection. When the ash bag 55 is full of dust, the staff can remove the ash bag 55 for replacement through the replacement assembly.
参照图5与图6,换装组件包括固定架6与横移座61,固定架6与收集转移箱5相连接,横移座61与固定架6的内侧壁滑移连接,横移座61沿水平方向滑移,横移座61的滑移方向与收集转移箱5的延伸方向相垂直,固定架6的侧壁设置有横移驱动件62,横移驱动件62为气缸,横移驱动件62的驱动端与横移座61的侧壁相连接,横移座61的顶侧插接有拆装架63,拆装架63的数量不低于两件,本实施例中,拆装架63的数量为两件,且拆装架63沿横移座61的滑移方向排列,可沿竖直向上的方向直线移动拆装架63,从而将拆装架63拆出横移座61,拆装架63的顶部呈环形架状,拆装架63的中部由多根直杆组成,拆装架63的底部呈环状,横移座61的顶侧开设有用于供拆装架63的顶部插入与滑移的阶梯通槽611,阶梯通槽611的数量与拆装架63的数量相一致,集灰袋55与拆装架63为可拆卸式连接。5 and 6, the replacement assembly includes a fixed frame 6 and a transverse seat 61, the fixed frame 6 is connected to the collection transfer box 5, the transverse seat 61 is slidably connected to the inner side wall of the fixed frame 6, the transverse seat 61 slides in the horizontal direction, and the sliding direction of the transverse seat 61 is perpendicular to the extension direction of the collection transfer box 5. The side wall of the fixed frame 6 is provided with a transverse driving member 62, the transverse driving member 62 is a cylinder, and the driving end of the transverse driving member 62 is connected to the side wall of the transverse seat 61. The top side of the transverse seat 61 is plugged with a disassembly frame 63, and the number of the disassembly frame 63 is not less than two. In this embodiment There are two disassembly and assembly frames 63, and the disassembly and assembly frames 63 are arranged along the sliding direction of the transverse displacement seat 61. The disassembly and assembly frames 63 can be moved linearly in the vertical upward direction to remove the disassembly and assembly frames 63 from the transverse displacement seat 61. The top of the disassembly and assembly frames 63 is in the shape of an annular frame, and the middle part of the disassembly and assembly frames 63 is composed of multiple straight rods. The bottom of the disassembly and assembly frames 63 is in the shape of an annular frame. The top side of the transverse displacement seat 61 is provided with a stepped through groove 611 for the top of the disassembly and assembly frames 63 to be inserted and slided. The number of the stepped through grooves 611 is consistent with the number of the disassembly and assembly frames 63, and the dust collecting bag 55 is detachably connected to the disassembly and assembly frames 63.
在进行步骤S2-S4的过程中,当其中一个集灰袋55装满时,令横移驱动件62驱使横移座61横移,更换另一个集灰袋55进行装灰,将装满灰的集灰袋55连通拆装架63拆出横移座61,然后将集灰袋55拆离拆装架63,更换新的集灰袋55装在拆装架63上,再将拆装架63重新安装在横移座61上,从而实现不间断收集粉尘的效果。During steps S2-S4, when one of the dust collecting bags 55 is full, the transverse driving component 62 drives the transverse moving seat 61 to move transversely, and another dust collecting bag 55 is replaced to be filled with dust. The dust collecting bag 55 filled with dust is connected to the disassembly frame 63 and removed from the transverse moving seat 61. Then, the dust collecting bag 55 is removed from the disassembly frame 63, and a new dust collecting bag 55 is replaced and installed on the disassembly frame 63. Then, the disassembly frame 63 is reinstalled on the transverse moving seat 61, thereby achieving the effect of uninterrupted dust collection.
固定架6的底部安装有起降驱动件64,起降驱动件64为气缸,起降驱动件64的驱动端连接有起降座65的底部,起降驱动件64可驱使起降座65沿竖直方向移动,拆装架63的底部连接有插环632,起降座65的顶部开设有用于供拆装架63底部的插环632插入的环形槽651,收集转移箱5出料端的底侧连接有固定座56,固定座56的底侧开设有贯穿到固定座56顶侧的空孔57,空孔57与收集转移箱5的出料端开口相对应连通,横移座61的顶侧与固定座56的底侧相靠近,空孔57的孔壁连接有扫架571,扫架571的底部设有扫毛572,扫毛572的底端高度位置低于横移座61的顶侧高度位置,固定架6与固定座56的底部相连接,拆装架63的顶部设有插块631,固定座56的底侧开设有可供插块631插入的插孔561,拆装架63的插块631与固定座56的底侧相插接,起降座65的顶部设置有压力传感器652,使用集灰袋55收集粉尘时,该集灰袋55的底部与压力传感器652相靠近,压力传感器652与起降驱动件64电连接。A lifting and lowering driving member 64 is installed at the bottom of the fixed frame 6. The lifting and lowering driving member 64 is a cylinder. The driving end of the lifting and lowering driving member 64 is connected to the bottom of the lifting and lowering seat 65. The lifting and lowering driving member 64 can drive the lifting and lowering seat 65 to move in the vertical direction. The bottom of the disassembly and assembly frame 63 is connected to the plug ring 632. The top of the lifting and lowering seat 65 is provided with an annular groove 651 for inserting the plug ring 632 at the bottom of the disassembly and assembly frame 63. The bottom side of the discharge end of the collection and transfer box 5 is connected to the fixed seat 56. The bottom side of the fixed seat 56 is provided with an empty hole 57 that penetrates to the top side of the fixed seat 56. The empty hole 57 is connected to the discharge end opening of the collection and transfer box 5. The top side of the transverse seat 61 is against the bottom side of the fixed seat 56. Nearly, the hole wall of the empty hole 57 is connected with a sweeping frame 571, and the bottom of the sweeping frame 571 is provided with a sweeping bristle 572, and the bottom end height position of the sweeping bristle 572 is lower than the top side height position of the transverse displacement seat 61, the fixed frame 6 is connected with the bottom of the fixed seat 56, the top of the disassembly frame 63 is provided with an insertion block 631, and the bottom side of the fixed seat 56 is provided with a socket 561 for the insertion of the insertion block 631, and the insertion block 631 of the disassembly frame 63 is plugged into the bottom side of the fixed seat 56, and a pressure sensor 652 is provided on the top of the lifting and lowering seat 65. When the dust collecting bag 55 is used to collect dust, the bottom of the dust collecting bag 55 is close to the pressure sensor 652, and the pressure sensor 652 is electrically connected to the lifting and lowering drive component 64.
集灰袋55装满粉尘时,集灰袋55膨胀变形,集灰袋55的底部对压力传感器652施加压力,压力传感器652感应到预期压力值,起降驱动件64驱使起降座65下降,令横移驱动件62驱使横移座61横移,更换另一个集灰袋55进行装灰,横移过程中,扫毛572可将落在横移座61顶侧的粉尘进行扫刮,将粉尘扫到需要进行装灰的集灰袋55中,从而减少粉尘留在横移座61顶侧导致被横移座61带出固定座56外的情况,减少粉尘外泄,减少工作环境受到的污染。When the dust collecting bag 55 is filled with dust, the dust collecting bag 55 expands and deforms, and the bottom of the dust collecting bag 55 applies pressure to the pressure sensor 652. The pressure sensor 652 senses the expected pressure value, and the lifting and lowering drive component 64 drives the lifting and lowering seat 65 to descend, so that the transverse driving component 62 drives the transverse seat 61 to move transversely, and replaces another dust collecting bag 55 for loading dust. During the transverse movement, the sweeping hair 572 can sweep the dust that falls on the top side of the transverse seat 61, and sweep the dust into the dust collecting bag 55 that needs to be loaded with dust, thereby reducing the dust remaining on the top side of the transverse seat 61 and being carried out of the fixed seat 56 by the transverse seat 61, reducing dust leakage, and reducing the pollution of the working environment.
集灰袋55与拆装架63为可拆卸式连接,集灰袋55位于拆装架63的内侧,集灰袋55的袋口设有连接环551,连接环551与插块631相插接,插块631穿过连接环551,更换集灰袋55时,将连接环551与集灰袋55向上取出即可。The ash bag 55 is detachably connected to the disassembly frame 63. The ash bag 55 is located on the inner side of the disassembly frame 63. A connecting ring 551 is provided at the bag opening of the ash bag 55. The connecting ring 551 is plugged into the plug block 631. The plug block 631 passes through the connecting ring 551. When replacing the ash bag 55, the connecting ring 551 and the ash bag 55 can be taken out upwards.
参照图3与图7,分离过滤箱3的内壁连接有隔板34,隔板34将过滤腔32与隔离室33相分隔,滤气组件包括若干滤尘袋341,滤尘袋341由玻纤针刺毡或不锈钢纤维针刺毡制成,隔板34的底侧开设有通气孔,滤尘袋341安装在通气孔处,分离过滤箱3的外侧连接有出风管35,出风管35与隔离室33相连通,步骤S4中,气体通过滤尘袋341过滤后进入隔离室33,然后从隔离室33进入出风管35,通过排风驱动件351将出风管35中的气体抽到排气囱4中,排风驱动件351为设置在出风管35外侧的风机,排风驱动件351的吸风端与出风管35相连通,排风驱动件351的排风端与排气囱4相连通。3 and 7 , a partition 34 is connected to the inner wall of the separation filter box 3, which separates the filter chamber 32 from the isolation chamber 33. The air filter assembly includes a plurality of dust bags 341, which are made of glass fiber needle felt or stainless steel fiber needle felt. A vent is provided on the bottom side of the partition 34, and the dust bags 341 are installed at the vent. An air outlet pipe 35 is connected to the outer side of the separation filter box 3, and the air outlet pipe 35 is connected to the isolation chamber 33. In step S4, the gas enters the isolation chamber 33 after being filtered by the dust bag 341, and then enters the air outlet pipe 35 from the isolation chamber 33. The gas in the air outlet pipe 35 is drawn into the exhaust chimney 4 through the exhaust drive 351. The exhaust drive 351 is a fan arranged on the outer side of the air outlet pipe 35. The suction end of the exhaust drive 351 is connected to the air outlet pipe 35, and the exhaust end of the exhaust drive 351 is connected to the exhaust chimney 4.
废气进入分离腔31进行二次沉降后,气体部分重量较轻,因此向上飘入过滤腔32,然后从滤尘袋341的外部穿入滤尘袋341的内部,再从通气孔进入到隔离室33中,而二次沉降后废气的细小粉尘被滤尘袋341阻挡,从而被阻留在滤尘袋341的外壁,此状态下隔离室33中的气体已完成颗粒粉尘的沉降与过滤,得到净化,可以进行排放,从而减少废气的排放,以达到环保效果,减少对空气的污染。After the exhaust gas enters the separation chamber 31 for secondary sedimentation, the gas part is lighter in weight, so it floats upward into the filter chamber 32, and then passes through the inside of the dust filter bag 341 from the outside, and then enters the isolation chamber 33 from the vent hole. The fine dust in the exhaust gas after the secondary sedimentation is blocked by the dust filter bag 341, and is thus retained on the outer wall of the dust filter bag 341. In this state, the gas in the isolation chamber 33 has completed the sedimentation and filtration of the particulate dust, and has been purified and can be discharged, thereby reducing the emission of exhaust gas, so as to achieve an environmental protection effect and reduce air pollution.
在步骤S4后加入步骤S5:启动脱尘驱动件39,通过通气孔对除尘室内的滤尘袋341的袋口进行间歇式喷气,脱尘驱动件39为风机或空压机,脱尘驱动件39安装在分离过滤箱3的外顶壁,脱尘驱动件39的出气端与通气孔位置相对应。Add step S5 after step S4: start the dust removal drive 39, and intermittently spray the bag opening of the dust filter bag 341 in the dust removal chamber through the vent. The dust removal drive 39 is a fan or an air compressor. The dust removal drive 39 is installed on the outer top wall of the separation filter box 3, and the air outlet end of the dust removal drive 39 corresponds to the position of the vent.
随着过滤时间增加,附着在滤尘袋341上的粉尘越来越多,增加滤尘袋341的透气阻力,使得可处理的气体量逐渐减少,因此令脱尘驱动件39间歇式对滤尘袋341进行吹气,空气瞬时地高速喷向滤尘袋341,同时诱导周边净气进入滤尘袋341,使滤尘袋341瞬间急剧膨胀,令积附在滤尘袋341表面的粉尘层脱落,滤尘袋341恢复过滤能力,脱落的粉尘落入分离腔31,然后掉入收集转移箱5中收集。As the filtering time increases, more and more dust adheres to the dust filter bag 341, which increases the air permeability resistance of the dust filter bag 341, causing the amount of gas that can be processed to gradually decrease. Therefore, the dust removal drive 39 is used to intermittently blow air to the dust filter bag 341, and the air is instantly sprayed to the dust filter bag 341 at high speed, while inducing the surrounding clean air to enter the dust filter bag 341, causing the dust filter bag 341 to expand sharply in an instant, causing the dust layer attached to the surface of the dust filter bag 341 to fall off, and the dust filter bag 341 restores its filtering capacity. The fallen dust falls into the separation chamber 31, and then falls into the collection transfer box 5 for collection.
参照图3与图8,滤气组件还包括外笼架342与内笼架343,外笼架342连接在隔板34的底部,内笼架343与滤尘袋341可拆卸式安装在隔板34的顶部,内笼架343与滤尘袋341穿过通气孔伸到过滤腔32中,外笼架342罩设在滤尘袋341的周侧,滤尘袋341位于外笼架342与内笼架343之间,滤尘袋341套设在内笼架343的外周侧。3 and 8 , the air filter assembly further includes an outer cage frame 342 and an inner cage frame 343. The outer cage frame 342 is connected to the bottom of the partition 34. The inner cage frame 343 and the dust filter bag 341 are detachably mounted on the top of the partition 34. The inner cage frame 343 and the dust filter bag 341 extend into the filter chamber 32 through the vent hole. The outer cage frame 342 is covered on the peripheral side of the dust filter bag 341. The dust filter bag 341 is located between the outer cage frame 342 and the inner cage frame 343. The dust filter bag 341 is sleeved on the outer peripheral side of the inner cage frame 343.
在过滤时,内笼架343对滤尘袋341的内侧进行支撑,阻碍滤尘袋341发生收缩,喷气时,外笼架342可对滤尘袋341的外侧进行限位,减少滤尘袋341过度膨胀变形的情况,减少风力过大时滤尘袋341与内笼架343发生撕扯的情况。During filtering, the inner cage frame 343 supports the inner side of the dust bag 341 to prevent the dust bag 341 from shrinking. During jetting, the outer cage frame 342 can limit the outer side of the dust bag 341 to reduce the excessive expansion and deformation of the dust bag 341 and the tearing between the dust bag 341 and the inner cage frame 343 when the wind is too strong.
隔板34的顶侧转动连接有转动环36,内笼架343的顶部呈环形架状,滤尘袋341的袋口与内笼架343的顶部通过螺栓安装在转动环36的顶部,滤尘袋341的袋口位于内笼架343的顶侧与转动环36之间,转动环36的侧壁连接有延伸杆361,隔板34的顶部设置有转动驱动件37,转动驱动件37为气缸,转动驱动件37的驱动端连接有驱动杆38,驱动杆38的侧壁通过转轴与延伸杆361远离转动环36的一端转动连接,驱动杆38与隔板34的顶侧滑移配合,驱动杆38滑移时可带动延伸杆361与转动环36转动。The top side of the partition 34 is rotatably connected with a rotating ring 36, the top of the inner cage frame 343 is in the shape of an annular frame, the bag opening of the dust filter bag 341 and the top of the inner cage frame 343 are installed on the top of the rotating ring 36 by bolts, the bag opening of the dust filter bag 341 is located between the top side of the inner cage frame 343 and the rotating ring 36, the side wall of the rotating ring 36 is connected with an extension rod 361, and a rotating driving member 37 is provided on the top of the partition 34. The rotating driving member 37 is a cylinder, and the driving end of the rotating driving member 37 is connected with a driving rod 38. The side wall of the driving rod 38 is rotatably connected with one end of the extension rod 361 away from the rotating ring 36 through a rotating shaft, and the driving rod 38 is slidably matched with the top side of the partition 34. When the driving rod 38 slides, it can drive the extension rod 361 and the rotating ring 36 to rotate.
需要清理滤尘袋341上的粉尘时,令转动驱动件37驱使驱动杆38滑移,通过带动延伸杆361带动转动环36进行转动,从而带动内笼架343与滤尘袋341进行转动,当滤尘袋341转动时,滤尘袋341的外侧与外笼架342的内侧发生摩擦,从而使外笼架342对滤尘袋341上的粉尘进行刮扫,使粉尘脱落,达到粉尘清理的效果。When it is necessary to clean the dust on the dust filter bag 341, the rotating driving member 37 drives the driving rod 38 to slide, and drives the extending rod 361 to drive the rotating ring 36 to rotate, thereby driving the inner cage frame 343 and the dust filter bag 341 to rotate. When the dust filter bag 341 rotates, the outer side of the dust filter bag 341 rubs against the inner side of the outer cage frame 342, so that the outer cage frame 342 scrapes the dust on the dust filter bag 341 to make the dust fall off, thereby achieving the effect of dust cleaning.
分离过滤箱3由一种混凝土浇筑而成,该混凝土具体如下:The separation filter box 3 is cast by a concrete, and the concrete is as follows:
本实施例中,还公开一种混凝土以及该混凝土的制备工艺。In this embodiment, a concrete and a preparation process of the concrete are also disclosed.
一种混凝土,原料包括300kg水泥、150kg粉煤灰、755kg连续级配为5-12mm的碎石,245kg铝渣、400kg细度模数为2.4-2.8的细砂、4kg减水剂、45kg有机硅改性丙烯酸乳液以及165kg水,其中,减水剂包括聚羧酸减水剂与木质素磺酸钠,聚羧酸减水剂与木质素磺酸钠的重量比为3:1;有机硅改性丙烯酸乳液采用北京互益型号为HBC-3000的有机硅改性丙烯酸乳液。A concrete, the raw materials of which include 300kg of cement, 150kg of fly ash, 755kg of crushed stone with continuous grading of 5-12mm, 245kg of aluminum slag, 400kg of fine sand with a fineness modulus of 2.4-2.8, 4kg of water reducer, 45kg of organosilicon modified acrylic emulsion and 165kg of water, wherein the water reducer includes polycarboxylate water reducer and sodium lignin sulfonate, and the weight ratio of the polycarboxylate water reducer to the sodium lignin sulfonate is 3:1; the organosilicon modified acrylic emulsion adopts the organosilicon modified acrylic emulsion with model HBC-3000 produced by Beijing Huyi.
混凝土的制备工艺包括以下步骤:The concrete preparation process includes the following steps:
Q1:将60kg水泥与33kg水均匀混合,得到粘结浆料;Q1: 60kg cement and 33kg water were uniformly mixed to obtain bonding slurry;
Q2:向粘结浆料中加入铝渣,搅拌均匀后,倒入磨具中干燥成型后破碎,制备粒径范围为5-12mm的预处理铝渣;Q2: Add aluminum slag to the bonding slurry, stir evenly, pour into the mold, dry, shape and crush, and prepare pretreated aluminum slag with a particle size range of 5-12mm;
Q3:将预处理铝渣投入有机硅改性丙烯酸乳液中,搅拌均匀后,静置30min,接着将预处理铝渣从有机硅改性丙烯酸乳液中分离出来,干燥后,得到含水率低于0.1%的改性铝渣;Q3: Add the pretreated aluminum slag into the silicone modified acrylic emulsion, stir evenly, and let it stand for 30 minutes. Then separate the pretreated aluminum slag from the silicone modified acrylic emulsion and dry it to obtain modified aluminum slag with a moisture content of less than 0.1%;
Q4:将减水剂与132kg水均匀混合,得到外加剂溶液;Q4: Evenly mix the water reducer with 132 kg of water to obtain an admixture solution;
Q5:将240kg水泥、粉煤灰加入外加剂溶液中,均匀混合,得到水泥浆料;Q5: Add 240kg of cement and fly ash into the admixture solution and mix evenly to obtain cement slurry;
Q6:将碎石、细砂以及改性铝渣加入水泥浆料中,搅拌均匀,得到混凝土。Q6: Add crushed stone, fine sand and modified aluminum slag into cement slurry, mix well to obtain concrete.
先采用水泥与水制得的粘结浆料对铝渣进行预改性,然后再采用有机硅改性丙烯酸乳液对铝渣进行改性,并控制改性铝渣的含水量低于0.1%,有利于获得氯离子迁移系数低、钢筋锈蚀失重率小且抗硫酸盐腐蚀性能好的耐腐蚀混凝土,可获得耐腐蚀性良好,能够在露天环境中长时间使用的混凝土。The aluminum slag is first pre-modified with a bonding slurry made of cement and water, and then modified with an organosilicon-modified acrylic emulsion, and the water content of the modified aluminum slag is controlled to be lower than 0.1%. This is conducive to obtaining corrosion-resistant concrete with a low chloride ion migration coefficient, a small steel bar corrosion weight loss rate and good sulfate corrosion resistance. It can obtain concrete with good corrosion resistance that can be used for a long time in an open air environment.
本申请实施例的实施原理为:通过两次沉降依次使废气中的金属颗粒以及粉尘等粗颗粒物从废气中分离,然后通过滤尘袋341将废气中剩余的细小颗粒粉尘与气体相互分离,从而完成气体的过滤净化,在排出气体时,可减少排出气体中携带的金属颗粒与粉尘,沉降与过滤过程中,废气与碎屑粉尘可得到充分的分离,可对减少过滤后排放的气体对环境的污染,从而达到环保排气的效果。The implementation principle of the embodiment of the present application is: through two sedimentation steps, the metal particles and coarse particles such as dust in the exhaust gas are separated from the exhaust gas in turn, and then the remaining fine particles of dust in the exhaust gas are separated from the gas through the dust filter bag 341, thereby completing the gas filtration and purification. When the gas is discharged, the metal particles and dust carried in the exhaust gas can be reduced. During the sedimentation and filtration process, the exhaust gas and debris dust can be fully separated, which can reduce the pollution of the gas discharged after filtration to the environment, thereby achieving the effect of environmentally friendly exhaust.
以上均为本申请的较佳实施例,本实施例仅是对本申请作出的解释,并非依次限制本申请的保护范围,故:凡依本申请的结构、形状、原理所做的等效变化,均应涵盖于本申请的保护范围之内。The above are all preferred embodiments of the present application. The embodiments are only explanations of the present application and do not limit the protection scope of the present application in turn. Therefore, all equivalent changes made according to the structure, shape, and principle of the present application should be covered within the protection scope of the present application.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410975175.8A CN118698269A (en) | 2024-07-19 | 2024-07-19 | An environmentally friendly dust removal and exhaust method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410975175.8A CN118698269A (en) | 2024-07-19 | 2024-07-19 | An environmentally friendly dust removal and exhaust method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN118698269A true CN118698269A (en) | 2024-09-27 |
Family
ID=92808910
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202410975175.8A Pending CN118698269A (en) | 2024-07-19 | 2024-07-19 | An environmentally friendly dust removal and exhaust method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN118698269A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201026426Y (en) * | 2007-02-12 | 2008-02-27 | 郑郁林 | Multifunctional bag filter |
| CN205340446U (en) * | 2015-12-24 | 2016-06-29 | 常州市新武机械有限公司 | Special dust remover of bituminous mixing plant |
| JP2016120453A (en) * | 2014-12-24 | 2016-07-07 | 株式会社フロム工業 | Solid-liquid separation and recovery device |
| CN207838506U (en) * | 2017-10-20 | 2018-09-11 | 惠州市金名豪家具有限公司 | A kind of wood cutting dust recycling and processing device |
| CN210543869U (en) * | 2019-08-29 | 2020-05-19 | 北京高安屯垃圾焚烧有限公司 | A bag filter |
| CN211196777U (en) * | 2019-08-07 | 2020-08-07 | 贵州迎祥米业有限公司 | Sieving mechanism is used in organic rice processing |
| CN115738515A (en) * | 2022-11-23 | 2023-03-07 | 江苏嫦娥环境科技有限公司 | Mechanical dust cleaning type bag dust collector |
-
2024
- 2024-07-19 CN CN202410975175.8A patent/CN118698269A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201026426Y (en) * | 2007-02-12 | 2008-02-27 | 郑郁林 | Multifunctional bag filter |
| JP2016120453A (en) * | 2014-12-24 | 2016-07-07 | 株式会社フロム工業 | Solid-liquid separation and recovery device |
| CN205340446U (en) * | 2015-12-24 | 2016-06-29 | 常州市新武机械有限公司 | Special dust remover of bituminous mixing plant |
| CN207838506U (en) * | 2017-10-20 | 2018-09-11 | 惠州市金名豪家具有限公司 | A kind of wood cutting dust recycling and processing device |
| CN211196777U (en) * | 2019-08-07 | 2020-08-07 | 贵州迎祥米业有限公司 | Sieving mechanism is used in organic rice processing |
| CN210543869U (en) * | 2019-08-29 | 2020-05-19 | 北京高安屯垃圾焚烧有限公司 | A bag filter |
| CN115738515A (en) * | 2022-11-23 | 2023-03-07 | 江苏嫦娥环境科技有限公司 | Mechanical dust cleaning type bag dust collector |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN220125738U (en) | Ore dressing dust processor | |
| JP2011224599A (en) | Cooling device of casting sand, and recovery treatment facility of casting sand | |
| CN107650297A (en) | The label impurity separator of plastic bottle piece | |
| CN118698269A (en) | An environmentally friendly dust removal and exhaust method | |
| CN205084545U (en) | Dust collector is retrieved in dust workshop | |
| CN208390122U (en) | A kind of paddy impurity separating device | |
| CN210965891U (en) | Metal powder separation dust collector | |
| CN219129949U (en) | Raw material pellet storage equipment for haydite sand preparation | |
| CN221907521U (en) | A recycling device for residual materials separated from concrete bricks | |
| CN218188543U (en) | Dust remover is used in industrial silicon processing | |
| CN106669970A (en) | Dry processing equipment for dedusting ash recycling of sintering machine head of iron and steel plant | |
| CN213375530U (en) | Plastic burning plate dust remover for collecting submicron powder | |
| CN104607391B (en) | Recovery Storage System | |
| CN218834067U (en) | Dust shaker that casting shop used | |
| CN211536890U (en) | Energy-concerving and environment-protective warehouse dust collector | |
| CN116196705B (en) | Anti-blocking clinker cement production line waste gas treatment device and method | |
| CN221847292U (en) | A glass micro-bead powder grinding machine | |
| CN219540967U (en) | Silicon carbide particle airflow cleaning equipment | |
| CN218053266U (en) | Environment-friendly concrete mixing plant | |
| CN217252750U (en) | Foundry waste sand regeneration treatment system | |
| CN220546710U (en) | Cloth bag dust remover for photovoltaic glass silica micropowder production line | |
| CN218250817U (en) | A collection device used in the process of removing ferromagnetic metal impurities from silicon powder | |
| CN223602838U (en) | A multi-functional dust removal device for basalt fiber production | |
| CN221999214U (en) | A bag dust collector for powder production | |
| CN221955367U (en) | A mineral powder rapid dust collection device for mineral powder 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 |