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CN110801678A - Dandelion-like self-dropping type filtering device for purifying heavily-polluted waste gas - Google Patents

Dandelion-like self-dropping type filtering device for purifying heavily-polluted waste gas Download PDF

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CN110801678A
CN110801678A CN201911131729.1A CN201911131729A CN110801678A CN 110801678 A CN110801678 A CN 110801678A CN 201911131729 A CN201911131729 A CN 201911131729A CN 110801678 A CN110801678 A CN 110801678A
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CN110801678B (en
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周孝银
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Wenling Yachaotong Shoes Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/56Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/58Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0002Casings; Housings; Frame constructions
    • B01D46/0005Mounting of filtering elements within casings, housings or frames
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0027Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
    • B01D46/0036Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/28Particle separators, e.g. dust precipitators, using filter brushes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42Auxiliary equipment or operation thereof
    • B01D46/4263Means for active heating or cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/60Combinations of devices covered by groups B01D46/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77Liquid phase processes
    • B01D53/78Liquid phase processes with gas-liquid contact

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Abstract

本发明公开了一种重污染废气净化用仿蒲公英自脱落式过滤装置,属于环保技术领域,可以实现模仿蒲公英的自脱落行为,将现有的过滤网单元化,以类似柔毛的分布形式展开,形成初步的空间过滤网,同时基于活性炭纤维材料的优异吸附性能,在过滤大粒径固体颗粒的同时,主动吸附废气含有的杂质和有害物质,配合后续的精细过滤处理实现不停机不降速的预过滤,同时采用润湿液体的方式,提高对废气的净化效果,针对废气特点选用合适的液体,不仅起到对废气的冷却作用,同时通过液体自身的滞留作用和对废气中有害物质的化学反应作用,进一步增加净化效果,同时在脱落后进行脱附处理,可以重复循环利用,符合可持续发展的环保理念。

Figure 201911131729

The invention discloses an imitation dandelion self-shedding filter device for purifying heavy polluted waste gas, belonging to the technical field of environmental protection, and can realize the self-shedding behavior of imitating the dandelion, unitize the existing filter screen, and deploy it in a distribution form similar to pilose At the same time, based on the excellent adsorption performance of activated carbon fiber material, it actively absorbs impurities and harmful substances contained in exhaust gas while filtering large-sized solid particles, and cooperates with subsequent fine filtration treatment to achieve non-stop and no speed reduction. At the same time, the method of wetting the liquid is used to improve the purification effect of the exhaust gas, and the appropriate liquid is selected according to the characteristics of the exhaust gas, which not only plays a role in cooling the exhaust gas, but also through the retention of the liquid itself and the harmful substances in the exhaust gas. The chemical reaction further increases the purification effect, and at the same time, the desorption treatment is carried out after falling off, which can be recycled and reused, which is in line with the environmental protection concept of sustainable development.

Figure 201911131729

Description

一种重污染废气净化用仿蒲公英自脱落式过滤装置A kind of dandelion-like self-shedding filter device for purification of heavily polluted waste gas

技术领域technical field

本发明涉及环保技术领域,更具体地说,涉及一种重污染废气净化用仿蒲公英自脱落式过滤装置。The invention relates to the technical field of environmental protection, and more particularly, to a dandelion-like self-dropping filter device for purification of heavily polluted waste gas.

背景技术Background technique

废气净化主要是指针对工业场所产生的工业废气诸如粉尘颗粒物、烟气烟尘、异味气体、有毒有害气体进行治理的工作。常见的废气净化有工厂烟尘废气净化、车间粉尘废气净化、有机废气净化、废气异味净化、酸碱废气净化、化工废气净化等。Exhaust gas purification mainly refers to the treatment of industrial waste gas such as dust particles, smoke and dust, odorous gases, and toxic and harmful gases generated in industrial places. Common waste gas purification includes factory dust and waste gas purification, workshop dust and waste gas purification, organic waste gas purification, waste gas odor purification, acid-base waste gas purification, chemical waste gas purification, etc.

废气的处理应从两方面进行:一是针对悬浮粒状污染物的废气除尘;二是针对气态污染物的废气净化气态污染物的控制主要是利用物化性质,如溶解度、吸附饱和度、露点及选择化学反应等的差异,将污染物从废气中分离出来;或者将污染物转化为无害或易于处理的物质。废气净化的基本方法有吸收法、吸附法、冷凝法、催化转化法及燃烧法等。The treatment of waste gas should be carried out from two aspects: one is the waste gas dust removal for suspended particulate pollutants; the other is the waste gas purification for gaseous pollutants. The control of gaseous pollutants mainly uses physicochemical properties, such as solubility, adsorption saturation, dew point and selective chemical properties. Differences in reactions, etc., to separate pollutants from exhaust gas; or to convert pollutants into harmless or easy-to-treat substances. The basic methods of exhaust gas purification include absorption method, adsorption method, condensation method, catalytic conversion method and combustion method.

大气污染的治理技术概述大气污染的治理技术是重要的大气环境保护对策措施,洁净燃烧技术是在燃烧过程减少污染物排放与提高燃料利用效率的加工、燃烧、转化和污染排放控制等所有技术的总称,二氧化硫、氮氧化物和烟(粉)尘是我国主要的大气污染物,减少二氧化硫、氮氧化物和烟(粉)尘的排放,对于保护和改善大气环境,不仅非常重要,而且十分紧迫。Overview of Air Pollution Control Technology Air pollution control technology is an important countermeasure for atmospheric environmental protection. Clean combustion technology is a process, combustion, transformation and pollution emission control technology that reduces pollutant emissions and improves fuel utilization efficiency in the combustion process. In general, sulfur dioxide, nitrogen oxides and smoke (powder) dust are the main air pollutants in my country. Reducing the emission of sulfur dioxide, nitrogen oxides and smoke (powder) dust is not only very important for protecting and improving the atmospheric environment, but also very urgent. .

而废弃净化中的先锋处理非过滤莫属,因此过滤的精细程度往往也决定了后续处理步骤的质量和难度,为此越来越多的过滤器涌现出来,提高对废气的过滤效果,但是重污染废气在过滤时的难度和要求更高,如果直接通过精细的过滤器来进行过滤的话,尽管具有较佳的过滤效果,例如工业废气净化中常用的布袋除尘器,对大颗粒杂质和烟尘的处理效果较佳,但是其主要是通过物理作用实现阻挡,而重污染废气的成分复杂且温度较高,直接通过布袋除尘器的话,一方面高温烟气直接接触会对其有一定的损伤,一般需要另外降温处理,另一方面大量固体颗粒和杂质会吸附在布袋除尘器表面影响废气的通过速率,降低过滤效果,需要停机或者其它处理手段恢复其过滤性能,这一过程往往占用大量时间,耽误废气净化的整体进度,另外就是在物理作用下的过滤效果一般,很多有毒气体等其它成分需要后续处理工艺另行处理,增加后续处理难度和时间。The pioneer treatment in waste purification is filtration. Therefore, the fineness of filtration often determines the quality and difficulty of subsequent treatment steps. For this reason, more and more filters have emerged to improve the filtration effect of exhaust gas, but it is important to It is more difficult and demanding to filter polluted waste gas. If it is filtered directly through a fine filter, although it has a better filtering effect, such as a bag filter commonly used in industrial waste gas purification, it is difficult to filter large particles of impurities and soot. The treatment effect is better, but it is mainly achieved through physical action, and the composition of the heavily polluted exhaust gas is complex and the temperature is high. Additional cooling treatment is required. On the other hand, a large number of solid particles and impurities will be adsorbed on the surface of the bag filter, affecting the passage rate of the exhaust gas, reducing the filtration effect, and requiring shutdown or other treatment methods to restore its filtration performance. This process often takes a lot of time and delays. The overall progress of exhaust gas purification, in addition, the filtration effect under physical action is general, and many other components such as toxic gases need to be treated separately by the subsequent treatment process, which increases the difficulty and time of subsequent treatment.

发明内容SUMMARY OF THE INVENTION

1.要解决的技术问题1. technical problem to be solved

针对现有技术中存在的问题,本发明的目的在于提供一种重污染废气净化用仿蒲公英自脱落式过滤装置,它可以实现模仿蒲公英的自脱落行为,将现有的过滤网单元化,以类似柔毛的分布形式展开,形成初步的空间过滤网,同时基于活性炭纤维材料的优异吸附性能,在过滤大粒径固体颗粒的同时,主动吸附废气含有的杂质和有害物质,为后续的废气净化降低处理难度,同时其是基于磁力连接的方式起到悬挂作用,待至吸附饱和后重量增大,抵抗磁力后产生脱落行为,不再阻挡废气的流通,配合后续的精细过滤处理实现不停机不降速的预过滤,同时采用润湿液体的方式,提高对废气的净化效果,针对废气特点选用合适的液体,不仅起到对废气的冷却作用,同时通过液体自身的滞留作用和对废气中有害物质的化学反应作用,进一步增加净化效果,同时在脱落后进行脱附处理,方便回收集中处理污染物,且可以重复循环利用,符合可持续发展的环保理念。In view of the problems existing in the prior art, the purpose of the present invention is to provide an imitation dandelion self-shedding filter device for the purification of heavy polluted waste gas, which can realize the self-shedding behavior of imitating the dandelion, unitize the existing filter screen, and The distribution form similar to pubescence is expanded to form a preliminary space filter. At the same time, based on the excellent adsorption performance of activated carbon fiber material, while filtering large-sized solid particles, it actively absorbs impurities and harmful substances contained in exhaust gas for subsequent exhaust gas purification. It reduces the difficulty of treatment, and at the same time, it plays a suspension role based on the magnetic connection. After the adsorption is saturated, the weight increases, and it will fall off after resisting the magnetic force. Speed reduction pre-filtering, and at the same time, wetting liquid is used to improve the purification effect of exhaust gas. Selecting suitable liquid according to the characteristics of exhaust gas not only plays a role in cooling the exhaust gas, but also through the retention effect of the liquid itself and is harmful to the exhaust gas. The chemical reaction of the substance further increases the purification effect, and at the same time, the desorption treatment is carried out after falling off, which is convenient for the recovery and centralized treatment of pollutants, and can be recycled and reused, which is in line with the environmental protection concept of sustainable development.

2.技术方案2. Technical solutions

为解决上述问题,本发明采用如下的技术方案。In order to solve the above problems, the present invention adopts the following technical solutions.

一种重污染废气净化用仿蒲公英自脱落式过滤装置,包括过滤箱体,所述过滤箱体侧壁上开凿有多个呈环形阵列分布的进气孔,所述过滤箱体内安装有自脱落式过滤组件,所述自脱落式过滤组件包括吸附基环和多个过滤单体,且多个过滤单体均匀分布在吸附基环下侧,所述吸附基环内侧设有多个呈网格分布的磁铁环,所述磁铁环上端固定连接有储液盒,相邻的所述储液盒之间固定连接有连接丝,且周向外侧的连接丝与吸附基环内端固定连接,所述过滤单体包括上下依次分布的磁吸根部、滞留茎部、发散冠部,所述发散冠部外端固定连接有多个均匀分布的过滤绒毛,且发散冠部与过滤绒毛之间一体成型,所述发散冠部外表面包裹有吸附球壳,所述过滤绒毛外表面包裹有吸附表层。An imitation dandelion self-dropping filter device for heavy pollution waste gas purification, comprising a filter box body, a plurality of air intake holes distributed in an annular array are drilled on the side wall of the filter box body, and a self-shedding filter box is installed in the filter box. The self-detaching filter assembly includes an adsorption base ring and a plurality of filter monomers, and the plurality of filter monomers are evenly distributed on the lower side of the adsorption base ring, and the inner side of the adsorption base ring is provided with a plurality of grids. Distributed magnet rings, the upper end of the magnet ring is fixedly connected with a liquid storage box, a connecting wire is fixedly connected between the adjacent liquid storage boxes, and the connecting wire on the outer side in the circumferential direction is fixedly connected with the inner end of the adsorption base ring, so The filter unit includes a magnetic suction root, a retention stem, and a diverging crown that are sequentially distributed up and down. The outer end of the diverging crown is fixedly connected with a plurality of evenly distributed filter fluff, and the diverging crown and the filter fluff are integrally formed. , the outer surface of the divergent crown is wrapped with an adsorption spherical shell, and the outer surface of the filter fluff is wrapped with an adsorption surface layer.

进一步的,所述储液盒内开凿有流通空腔,所述磁铁环内端开凿有与流通空腔相连通的流道,其中一个所述储液盒上端固定连通有进液管,所述进液管远离储液盒一端安装有增压泵,所述储液盒下端开凿有滴液孔,所述滞留茎部内端开凿有与磁吸根部相匹配的顺液孔,所述发散冠部内端开凿有与顺液孔相连通的球形储液腔,所述发散冠部上开凿有多个均匀分布的导液微孔,可以实现根据重污染废气的特性从外部添加合适的液体,例如废气中二氧化硫含量较高,可以添加适量的碱性溶液,用来中和废气中的二氧化硫,提高废气净化效果,同时液体本身对烟尘具有一定的降温效果和滞留效果,提升对废气的过滤效果。Further, a circulation cavity is excavated in the liquid storage box, and a flow channel that communicates with the circulation cavity is excavated at the inner end of the magnet ring. A booster pump is installed at one end of the liquid inlet pipe away from the liquid storage box, a drip hole is drilled at the lower end of the liquid storage box, and a liquid drop hole matching the magnetic suction root is drilled at the inner end of the retention stem. There is a spherical liquid storage cavity connected to the liquid hole at the end, and a plurality of evenly distributed liquid-conducting micro-holes are drilled on the diverging crown, which can realize the addition of suitable liquid from the outside according to the characteristics of heavily polluted exhaust gas, such as exhaust gas The content of sulfur dioxide in the medium is relatively high, and an appropriate amount of alkaline solution can be added to neutralize the sulfur dioxide in the exhaust gas and improve the purification effect of the exhaust gas.

进一步的,所述磁铁环的内径大于磁吸根部的内径小于磁吸根部的外径,所述磁铁环下端固定连接有与磁吸根部相匹配的纠偏环,且纠偏环的内径略大于磁吸根部的外径,纠偏环起到对磁吸根部的磁吸导向作用,防止出现磁吸根部和磁铁环出现严重错位的现象,进而导致液体无法从磁铁环流至磁吸根部内完成后续的润湿工作。Further, the inner diameter of the magnet ring is larger than the inner diameter of the magnetic root and smaller than the outer diameter of the magnetic root, the lower end of the magnet ring is fixedly connected with a deviation correction ring matching the magnetic root, and the inner diameter of the deviation correction ring is slightly larger than the magnetic root. The outer diameter of the root, the correction ring plays a role in guiding the magnetic suction of the magnetic suction root, preventing the phenomenon of serious misalignment between the magnetic suction root and the magnet ring, and thus causing the liquid to fail to flow from the magnet ring to the magnetic suction root to complete the subsequent wetting. Work.

进一步的,所述磁吸根部采用铁磁性金属材料制成,所述磁铁环下端涂覆有纳米防水层,且磁铁环对磁吸根部的磁吸力略大于过滤单体的重力,可以保证磁铁环在正常状态吸附住过滤单体不至于脱落,纳米防水层的作用一方面可以避免液体的泄漏,另外一方面可以利用液体的表面张力提高对磁吸根部的吸附力。Further, the magnetic suction root is made of ferromagnetic metal material, the lower end of the magnet ring is coated with a nano-waterproof layer, and the magnetic suction force of the magnet ring to the magnetic suction root is slightly greater than the gravity of the filter unit, which can ensure the magnet ring. In the normal state, the filter monomer will not fall off. On the one hand, the function of the nano waterproof layer can avoid the leakage of the liquid, and on the other hand, the surface tension of the liquid can be used to improve the adsorption force of the magnetic suction root.

进一步的,所述滞留茎部外端开凿有多个吸附微孔,所述吸附微孔内设置有相贴合的膨润土吸附层,由于滞留茎部相对于磁吸根部之间的空间更大,废气在经过磁吸根部形成的空间网络结构后由于气压原因,会出现膨胀流向吸附微孔的现象,因此设置的膨润土吸附层可以直接吸附漏率的固体颗粒,提高过滤效果,同时延长废气的滞留时间,使得过滤绒毛的吸附可以更加充分。Further, the outer end of the retention stem is drilled with a plurality of adsorption micropores, and the adsorption micropores are provided with a bentonite adsorption layer that fits together. Because the space between the retention stems is larger than the magnetic roots, After the exhaust gas passes through the space network structure formed by the magnetic suction root, due to the air pressure, it will expand and flow to the adsorption micropores. Therefore, the bentonite adsorption layer set can directly adsorb the solid particles of the leakage rate, improve the filtering effect, and prolong the retention of exhaust gas at the same time. time, so that the adsorption of the filter fluff can be more sufficient.

进一步的,所述滞留茎部、发散冠部和过滤绒毛均采用轻质塑料制成,所述吸附球壳和吸附表层均采用活性炭纤维材料,所述活性炭纤维的直径为5-20μm,比表面积为1000-1500m2/g,平均孔径为1.0-4.0nm,活性炭纤维具有比粒状活性碳更大的吸附容量和更快的吸附动力学性能,在液相、气相中对有机物和阴、阳离子吸附效率高,吸、脱附速度快,可再生循环使用,同时耐酸、碱,耐高温,适应性强,导电性和化学稳定性好,是一种比较理想的环保材料。Further, the retention stem, the diverging crown and the filter fluff are all made of light plastic, and the adsorption spherical shell and the adsorption surface layer are all made of activated carbon fiber material, the diameter of the activated carbon fiber is 5-20 μm, and the specific surface area is 5-20 μm. It is 1000-1500m2/g, and the average pore size is 1.0-4.0nm. The activated carbon fiber has a larger adsorption capacity and faster adsorption kinetics than granular activated carbon. High, fast absorption and desorption speed, recyclable, acid and alkali resistance, high temperature resistance, strong adaptability, good electrical conductivity and chemical stability, is an ideal environmental protection material.

进一步的,所述发散冠部的半径与过滤绒毛的长度比为1:2-8,给过滤绒毛预留充分的吸附空间,在提高废气通过速率的同时提高过滤效率和质量,避免发散冠部占用太多空间阻挡废气的通过。Further, the ratio of the radius of the divergent crown to the length of the filter fluff is 1:2-8, and sufficient adsorption space is reserved for the filter fluff, which improves the filtration efficiency and quality while improving the exhaust gas passing rate, and avoids the divergent crown. Take up too much space to block the passage of exhaust gas.

进一步的,相邻的一对所述过滤单体之间的最短距离正好是过滤绒毛长度的两倍,可以使得过滤绒毛形成饱满严密无空隙的空间过滤网形式,提高过滤效果,不易出现过滤死角。Further, the shortest distance between an adjacent pair of the filter monomers is exactly twice the length of the filter fluff, which can make the filter fluff form a full, tight and void-free space filter screen, improve the filtering effect, and be less prone to filter dead ends. .

进一步的,所述吸附基环下侧设有回收平台,所述回收平台内安装有电磁铁,所述过滤箱体内侧壁上开凿有一对竖直且对称分布的升降槽,所述升降槽内安装有电动滑台,所述电动滑台上的电动滑块与回收平台之间固定连接,可以收集脱落后的过滤单体进行集中脱附处理,同时在处理完成后直接送到吸附基环下侧,利用磁吸作用自动吸附安装完成复位,重新循环利用继续过滤。Further, a recovery platform is arranged on the lower side of the adsorption base ring, an electromagnet is installed in the recovery platform, and a pair of vertical and symmetrically distributed lifting grooves are excavated on the inner side wall of the filter box. An electric sliding table is installed, and the electric sliding block on the electric sliding table is fixedly connected with the recovery platform, which can collect the filter unit after falling off for centralized desorption treatment, and directly send it to the adsorption base ring after the treatment is completed. On the side, the magnetic attraction is used to automatically absorb the installation to complete the reset, and then recycle and continue to filter.

进一步的,所述自脱落式过滤组件的数量可以为多个,不同所述自脱落式过滤组件的过滤单体尺寸保持差异,且自上至下尺寸逐渐增大,技术人员可以根据现场待过滤废气的实际情况选择合适的自脱落式过滤组件数量,理论上越多过滤效果越好,但是过滤速度有所下降,应当按照实际情况作出合理调整。Further, the number of the self-dropping filter assemblies can be multiple, and the size of the filter cells of different self-dropping filter assemblies is kept different, and the size gradually increases from top to bottom. The actual situation of the exhaust gas selects the appropriate number of self-dropping filter components. In theory, the more the filtering effect, the better the filtering effect, but the filtering speed has decreased, and should be adjusted reasonably according to the actual situation.

3.有益效果3. beneficial effect

相比于现有技术,本发明的优点在于:Compared with the prior art, the advantages of the present invention are:

(1)本方案可以实现模仿蒲公英的自脱落行为,将现有的过滤网单元化,以类似柔毛的分布形式展开,形成初步的空间过滤网,同时基于活性炭纤维材料的优异吸附性能,在过滤大粒径固体颗粒的同时,主动吸附废气含有的杂质和有害物质,为后续的废气净化降低处理难度,同时其是基于磁力连接的方式起到悬挂作用,待至吸附饱和后重量增大,抵抗磁力后产生脱落行为,不再阻挡废气的流通,配合后续的精细过滤处理实现不停机不降速的预过滤,同时采用润湿液体的方式,提高对废气的净化效果,针对废气特点选用合适的液体,不仅起到对废气的冷却作用,同时通过液体自身的滞留作用和对废气中有害物质的化学反应作用,进一步增加净化效果,同时在脱落后进行脱附处理,方便回收集中处理污染物,且可以重复循环利用,符合可持续发展的环保理念。(1) This scheme can imitate the self-shedding behavior of dandelion, unitize the existing filter, and expand it in a distribution form similar to pilose to form a preliminary spatial filter. At the same time, based on the excellent adsorption performance of activated carbon fiber While filtering large-sized solid particles, it actively adsorbs impurities and harmful substances contained in the exhaust gas, reducing the difficulty of treatment for subsequent exhaust gas purification. At the same time, it plays a suspension role based on the magnetic connection. After the adsorption is saturated, the weight increases. After resisting the magnetic force, the shedding behavior will occur, and the flow of exhaust gas will no longer be blocked. With the follow-up fine filtration treatment, the pre-filtration can be realized without stopping the machine and reducing the speed. At the same time, the method of wetting the liquid is used to improve the purification effect of the exhaust gas. The liquid not only cools the exhaust gas, but also further increases the purification effect through the retention of the liquid itself and the chemical reaction of harmful substances in the exhaust gas. , and can be recycled and reused, which is in line with the environmental protection concept of sustainable development.

(2)储液盒内开凿有流通空腔,磁铁环内端开凿有与流通空腔相连通的流道,其中一个储液盒上端固定连通有进液管,进液管远离储液盒一端安装有增压泵,储液盒下端开凿有滴液孔,滞留茎部内端开凿有与磁吸根部相匹配的顺液孔,发散冠部内端开凿有与顺液孔相连通的球形储液腔,发散冠部上开凿有多个均匀分布的导液微孔,可以实现根据重污染废气的特性从外部添加合适的液体,例如废气中二氧化硫含量较高,可以添加适量的碱性溶液,用来中和废气中的二氧化硫,提高废气净化效果,同时液体本身对烟尘具有一定的降温效果和滞留效果,提升对废气的过滤效果。(2) A circulation cavity is excavated in the liquid storage box, and a flow channel that communicates with the circulation cavity is excavated at the inner end of the magnet ring. A liquid inlet pipe is fixedly connected to the upper end of one of the liquid storage boxes, and the liquid inlet pipe is away from the end of the liquid storage box. A booster pump is installed, a drip hole is drilled at the lower end of the liquid storage box, a liquid drop hole matching the magnetic suction root is drilled at the inner end of the retention stem, and a spherical liquid storage cavity that communicates with the drop hole is drilled at the inner end of the diverging crown. , There are a number of evenly distributed liquid-conducting micro-holes drilled on the diverging crown, which can add appropriate liquid from the outside according to the characteristics of heavily polluted exhaust gas. For example, the sulfur dioxide content in the exhaust gas is high, and an appropriate amount of alkaline solution can be added to It neutralizes the sulfur dioxide in the exhaust gas and improves the purification effect of the exhaust gas. At the same time, the liquid itself has a certain cooling effect and retention effect on the smoke and dust, which improves the filtering effect of the exhaust gas.

(3)磁铁环的内径大于磁吸根部的内径小于磁吸根部的外径,磁铁环下端固定连接有与磁吸根部相匹配的纠偏环,且纠偏环的内径略大于磁吸根部的外径,纠偏环起到对磁吸根部的磁吸导向作用,防止出现磁吸根部和磁铁环出现严重错位的现象,进而导致液体无法从磁铁环流至磁吸根部内完成后续的润湿工作。(3) The inner diameter of the magnet ring is larger than the inner diameter of the magnetic root and smaller than the outer diameter of the magnetic root. The lower end of the magnet ring is fixedly connected with a correction ring matching the magnetic root, and the inner diameter of the correction ring is slightly larger than the outer diameter of the magnetic root. , the deviation correction ring plays a role in guiding the magnetic suction of the magnetic suction root, preventing the phenomenon of serious misalignment between the magnetic suction root and the magnet ring, and then the liquid cannot flow from the magnet circulation to the magnetic suction root to complete the subsequent wetting work.

(4)磁吸根部采用铁磁性金属材料制成,磁铁环下端涂覆有纳米防水层,且磁铁环对磁吸根部的磁吸力略大于过滤单体的重力,可以保证磁铁环在正常状态吸附住过滤单体不至于脱落,纳米防水层的作用一方面可以避免液体的泄漏,另外一方面可以利用液体的表面张力提高对磁吸根部的吸附力。(4) The magnetic suction root is made of ferromagnetic metal material, the lower end of the magnet ring is coated with a nano waterproof layer, and the magnetic suction force of the magnet ring to the magnetic suction root is slightly greater than the gravity of the filter unit, which can ensure that the magnet ring is adsorbed in a normal state Keep the filter monomer from falling off. On the one hand, the role of the nano-waterproof layer can avoid the leakage of the liquid, and on the other hand, the surface tension of the liquid can be used to improve the adsorption force of the magnetic root.

(5)滞留茎部外端开凿有多个吸附微孔,吸附微孔内设置有相贴合的膨润土吸附层,由于滞留茎部相对于磁吸根部之间的空间更大,废气在经过磁吸根部形成的空间网络结构后由于气压原因,会出现膨胀流向吸附微孔的现象,因此设置的膨润土吸附层可以直接吸附漏率的固体颗粒,提高过滤效果,同时延长废气的滞留时间,使得过滤绒毛的吸附可以更加充分。(5) A plurality of adsorption micropores are drilled at the outer end of the retention stem, and a bentonite adsorption layer is arranged in the adsorption micropore. Since the space between the retention stems is larger than that between the magnetic roots, the exhaust gas passes through the magnetic adsorption. After the space network structure formed by the root is sucked, due to the air pressure, the phenomenon of expansion and flow to the adsorption pores will occur. Therefore, the bentonite adsorption layer set can directly absorb the solid particles of the leakage rate, improve the filtration effect, and prolong the residence time of the exhaust gas, so that the filtration The adsorption of fluff can be more sufficient.

(6)滞留茎部、发散冠部和过滤绒毛均采用轻质塑料制成,吸附球壳和吸附表层均采用活性炭纤维材料,活性炭纤维的直径为5-20μm,比表面积为1000-1500m2/g,平均孔径为1.0-4.0nm,活性炭纤维具有比粒状活性碳更大的吸附容量和更快的吸附动力学性能,在液相、气相中对有机物和阴、阳离子吸附效率高,吸、脱附速度快,可再生循环使用,同时耐酸、碱,耐高温,适应性强,导电性和化学稳定性好,是一种比较理想的环保材料。(6) The retention stem, divergent crown and filter fluff are all made of lightweight plastic, and the adsorption spherical shell and adsorption surface are made of activated carbon fiber material. The diameter of the activated carbon fiber is 5-20 μm, and the specific surface area is 1000-1500m2/g , the average pore size is 1.0-4.0nm, activated carbon fiber has larger adsorption capacity and faster adsorption kinetics than granular activated carbon, high adsorption efficiency for organic matter and anion and cation in liquid and gas phase, adsorption, desorption It has high speed, can be regenerated and recycled, and is resistant to acid, alkali, high temperature, strong adaptability, good electrical conductivity and chemical stability. It is an ideal environmental protection material.

(7)发散冠部的半径与过滤绒毛的长度比为1:2-8,给过滤绒毛预留充分的吸附空间,在提高废气通过速率的同时提高过滤效率和质量,避免发散冠部占用太多空间阻挡废气的通过。(7) The ratio of the radius of the divergent crown to the length of the filter fluff is 1:2-8, and sufficient adsorption space is reserved for the filter fluff, which improves the filtration efficiency and quality while improving the exhaust gas passing rate, and avoids the divergent crown occupying too much. Multiple spaces block the passage of exhaust gas.

(8)相邻的一对过滤单体之间的最短距离正好是过滤绒毛长度的两倍,可以使得过滤绒毛形成饱满严密无空隙的空间过滤网形式,提高过滤效果,不易出现过滤死角。(8) The shortest distance between the adjacent pair of filter monomers is exactly twice the length of the filter fluff, which can make the filter fluff form a full, tight and void-free space filter screen, improve the filtering effect, and be less prone to filter dead corners.

(9)吸附基环下侧设有回收平台,回收平台内安装有电磁铁,过滤箱体内侧壁上开凿有一对竖直且对称分布的升降槽,升降槽内安装有电动滑台,电动滑台上的电动滑块与回收平台之间固定连接,可以收集脱落后的过滤单体进行集中脱附处理,同时在处理完成后直接送到吸附基环下侧,利用磁吸作用自动吸附安装完成复位,重新循环利用继续过滤。(9) There is a recovery platform on the lower side of the adsorption base ring, an electromagnet is installed in the recovery platform, a pair of vertical and symmetrically distributed lifting grooves are excavated on the inner side wall of the filter box, and an electric sliding table is installed in the lifting groove. The electric slider on the table is fixedly connected with the recovery platform, which can collect the detached filter monomer for centralized desorption treatment, and at the same time, after the treatment is completed, it is directly sent to the lower side of the adsorption base ring, and the automatic adsorption and installation are completed by the magnetic attraction. Reset, recycle and continue filtering.

(10)自脱落式过滤组件的数量可以为多个,不同自脱落式过滤组件的过滤单体尺寸保持差异,且自上至下尺寸逐渐增大,技术人员可以根据现场待过滤废气的实际情况选择合适的自脱落式过滤组件数量,理论上越多过滤效果越好,但是过滤速度有所下降,应当按照实际情况作出合理调整。(10) The number of self-dropping filter components can be multiple. The size of the filter unit of different self-dropping filter components remains different, and the size gradually increases from top to bottom. The technician can according to the actual situation of the waste gas to be filtered on site Select the appropriate number of self-detaching filter components. In theory, the more the filtering effect, the better the filtering effect, but the filtering speed is reduced, and reasonable adjustments should be made according to the actual situation.

附图说明Description of drawings

图1为本发明的结构示意图;Fig. 1 is the structural representation of the present invention;

图2为本发明过滤单体部分过滤状态下的结构示意图;Fig. 2 is the structural representation under the filtering state of filter monomer part of the present invention;

图3为本发明吸附基环部分的俯视图;Fig. 3 is the top view of the adsorption base ring part of the present invention;

图4为本发明过滤单体部分的内部结构示意图;Fig. 4 is the internal structure schematic diagram of the filter monomer part of the present invention;

图5为本发明过滤绒毛的结构示意图。FIG. 5 is a schematic diagram of the structure of the filter fluff of the present invention.

图中标号说明:Description of the labels in the figure:

1过滤箱体、2吸附基环、3过滤单体、31磁吸根部、32滞留茎部、33发散冠部、34过滤绒毛、4回收平台、5电磁铁、6电动滑台、7进液管、8增压泵、9磁铁环、10储液盒、11连接丝、12吸附微孔、13吸附球壳、14吸附表层、15纠偏环。1 filter box, 2 adsorption base ring, 3 filter unit, 31 magnetic suction root, 32 retention stem, 33 divergent crown, 34 filter fluff, 4 recovery platform, 5 electromagnet, 6 electric sliding table, 7 liquid inlet Tube, 8 booster pump, 9 magnet ring, 10 liquid storage box, 11 connecting wire, 12 adsorption micropore, 13 adsorption spherical shell, 14 adsorption surface layer, 15 deviation correction ring.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述;显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例,基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention; obviously, the described embodiments are only a part of the embodiments of the present invention, not all of the embodiments. The embodiments of the present invention, and all other embodiments obtained by those of ordinary skill in the art without creative work, fall within the protection scope of the present invention.

在本发明的描述中,需要说明的是,术语“上”、“下”、“内”、“外”、“顶/底端”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that the orientations or positional relationships indicated by the terms "upper", "lower", "inner", "outer", "top/bottom", etc. are based on the orientations shown in the accompanying drawings Or the positional relationship is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and should not be construed to indicate or imply relative importance.

在本发明的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“设置有”、“套设/接”、“连接”等,应做广义理解,例如“连接”,可以是固定连接,也可以是可拆卸连接,或一体地连接,可以是机械连接,也可以是电连接,可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通,对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that, unless otherwise expressly specified and limited, the terms "installation", "provided with", "sleeve/connection", "connection", etc., should be understood in a broad sense, such as " Connection", which can be a fixed connection, a detachable connection, or an integral connection, a mechanical connection, an electrical connection, a direct connection, or an indirect connection through an intermediate medium, or an internal connection between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood in specific situations.

实施例1:Example 1:

请参阅图1-3,一种重污染废气净化用仿蒲公英自脱落式过滤装置,包括过滤箱体1,过滤箱体1侧壁上开凿有多个呈环形阵列分布的进气孔,过滤箱体1内安装有自脱落式过滤组件,自脱落式过滤组件包括吸附基环2和多个过滤单体3,且多个过滤单体3均匀分布在吸附基环2下侧,吸附基环2内侧设有多个呈网格分布的磁铁环9,磁铁环9上端固定连接有储液盒10,相邻的储液盒10之间固定连接有连接丝11,且周向外侧的连接丝11与吸附基环2内端固定连接,过滤单体3包括上下依次分布的磁吸根部31、滞留茎部32、发散冠部33,发散冠部33外端固定连接有多个均匀分布的过滤绒毛34,且发散冠部33与过滤绒毛34之间一体成型,过滤绒毛34起到定形的作用,避免柔性带来气流冲击出现变形孔隙的现象,发散冠部33外表面包裹有吸附球壳13,过滤绒毛34外表面包裹有吸附表层14。Please refer to Figure 1-3, a dandelion-like self-falling filter device for heavy pollution exhaust gas purification, including a filter box 1, a plurality of air intake holes distributed in an annular array are drilled on the side wall of the filter box 1, and the filter box The body 1 is equipped with a self-dropping filter assembly, the self-dropping filter assembly includes an adsorption base ring 2 and a plurality of filter units 3, and the plurality of filter units 3 are evenly distributed on the lower side of the adsorption base ring 2, and the adsorption base ring 2 The inner side is provided with a plurality of magnet rings 9 distributed in a grid. The upper end of the magnet ring 9 is fixedly connected with a liquid storage box 10, and a connecting wire 11 is fixedly connected between the adjacent liquid storage boxes 10, and the connecting wire 11 on the outer side in the circumferential direction is fixed. It is fixedly connected with the inner end of the adsorption base ring 2, and the filter unit 3 includes a magnetic suction root 31, a retention stem 32, and a diverging crown 33 that are sequentially distributed up and down. The outer end of the diverging crown 33 is fixedly connected with a plurality of uniformly distributed filter fluff. 34, and the divergent crown 33 and the filter fluff 34 are integrally formed, and the filter fluff 34 plays a role in setting the shape to avoid the phenomenon of deformed pores caused by airflow impact caused by flexibility, and the outer surface of the divergent crown 33 is wrapped with an adsorption spherical shell 13, The outer surface of the filter fluff 34 is wrapped with the adsorption surface layer 14 .

相邻的一对过滤单体3之间的最短距离正好是过滤绒毛34长度的两倍,可以使得过滤绒毛34形成饱满严密无空隙的空间过滤网形式,提高过滤效果,不易出现过滤死角。The shortest distance between the adjacent pair of filter units 3 is exactly twice the length of the filter fluff 34, which can make the filter fluff 34 form a full, tight and void-free space filter screen, improve the filtering effect, and be less prone to filter dead corners.

磁铁环9的内径大于磁吸根部31的内径小于磁吸根部31的外径,磁铁环9下端固定连接有与磁吸根部31相匹配的纠偏环15,且纠偏环15的内径略大于磁吸根部31的外径,纠偏环15起到对磁吸根部31的磁吸导向作用,防止出现磁吸根部31和磁铁环9出现严重错位的现象,进而导致液体无法从磁铁环9流至磁吸根部31内完成后续的润湿工作,磁吸根部31采用铁磁性金属材料制成,磁铁环9下端涂覆有纳米防水层,且磁铁环9对磁吸根部31的磁吸力略大于过滤单体3的重力,可以保证磁铁环9在正常状态吸附住过滤单体3不至于脱落,纳米防水层的作用一方面可以避免液体的泄漏,另外一方面可以利用液体的表面张力提高对磁吸根部31的吸附力,滞留茎部32外端开凿有多个吸附微孔12,吸附微孔12内设置有相贴合的膨润土吸附层,由于滞留茎部32相对于磁吸根部31之间的空间更大,废气在经过磁吸根部31形成的空间网络结构后由于气压原因,会出现膨胀流向吸附微孔12的现象,因此设置的膨润土吸附层可以直接吸附漏率的固体颗粒,提高过滤效果,同时延长废气的滞留时间,使得过滤绒毛34的吸附可以更加充分,滞留茎部32、发散冠部33和过滤绒毛34均采用轻质塑料制成,吸附球壳13和吸附表层14均采用活性炭纤维材料,活性炭纤维的直径为5-20μm,比表面积为1000-1500m2/g,平均孔径为1.0-4.0nm,活性炭纤维具有比粒状活性碳更大的吸附容量和更快的吸附动力学性能,在液相、气相中对有机物和阴、阳离子吸附效率高,吸、脱附速度快,可再生循环使用,同时耐酸、碱,耐高温,适应性强,导电性和化学稳定性好,是一种比较理想的环保材料,发散冠部33的半径与过滤绒毛34的长度比为1:2-8,给过滤绒毛34预留充分的吸附空间,在提高废气通过速率的同时提高过滤效率和质量,避免发散冠部33占用太多空间阻挡废气的通过。The inner diameter of the magnet ring 9 is larger than the inner diameter of the magnetic suction root 31 and smaller than the outer diameter of the magnetic suction root 31. The lower end of the magnet ring 9 is fixedly connected with a deviation correction ring 15 that matches the magnetic suction root 31, and the inner diameter of the deviation correction ring 15 is slightly larger than that of the magnetic suction root. The outer diameter of the root portion 31, the deflection correction ring 15 plays a role in guiding the magnetic attraction of the magnetic attraction root portion 31, preventing the phenomenon of serious misalignment between the magnetic attraction root portion 31 and the magnet ring 9, and then the liquid cannot flow from the magnet ring 9 to the magnetic attraction. The subsequent wetting work is completed in the root portion 31. The magnetic suction root portion 31 is made of ferromagnetic metal material. The lower end of the magnet ring 9 is coated with a nano waterproof layer, and the magnetic attraction force of the magnet ring 9 to the magnetic suction root portion 31 is slightly greater than that of the filter unit. The gravity of 3 can ensure that the magnet ring 9 adsorbs the filter unit 3 in a normal state and will not fall off. On the one hand, the role of the nano waterproof layer can avoid the leakage of the liquid, and on the other hand, the surface tension of the liquid can be used to improve the magnetic suction root 31. The outer end of the retention stem 32 is drilled with a plurality of adsorption micropores 12, and a bentonite adsorption layer is arranged in the adsorption micropore 12. Since the retention stem 32 is relatively smaller than the space between the magnetic roots 31 Due to the air pressure, the exhaust gas will expand and flow to the adsorption micropores 12 after passing through the spatial network structure formed by the magnetic suction root 31. Therefore, the bentonite adsorption layer set can directly adsorb the solid particles with the leakage rate, improve the filtering effect, and at the same time Extend the retention time of the exhaust gas, so that the adsorption of the filter fluff 34 can be more sufficient, the retention stem 32, the diverging crown 33 and the filter fluff 34 are all made of light plastic, and the adsorption spherical shell 13 and the adsorption surface layer 14 are made of activated carbon fiber material , the diameter of activated carbon fiber is 5-20μm, the specific surface area is 1000-1500m2/g, and the average pore size is 1.0-4.0nm. The activated carbon fiber has a larger adsorption capacity and faster adsorption kinetics than granular activated carbon. In the phase and gas phase, the adsorption efficiency of organic matter and anion and cation is high, the adsorption and desorption speed is fast, it can be recycled and used, and it is resistant to acid, alkali, high temperature, strong adaptability, good electrical conductivity and chemical stability. Ideal environmental protection material, the ratio of the radius of the diverging crown 33 to the length of the filter fluff 34 is 1:2-8, and sufficient adsorption space is reserved for the filter fluff 34 to improve the filtration efficiency and quality while improving the exhaust gas passing rate, avoiding The diverging crown 33 takes up too much space to block the passage of exhaust gases.

请参阅图4,储液盒10内开凿有流通空腔,磁铁环9内端开凿有与流通空腔相连通的流道,其中一个储液盒10上端固定连通有进液管7,进液管7远离储液盒10一端安装有增压泵8,储液盒10下端开凿有滴液孔,滞留茎部32内端开凿有与磁吸根部31相匹配的顺液孔,发散冠部33内端开凿有与顺液孔相连通的球形储液腔,发散冠部33上开凿有多个均匀分布的导液微孔,可以实现根据重污染废气的特性从外部添加合适的液体,例如废气中二氧化硫含量较高,可以添加适量的碱性溶液,用来中和废气中的二氧化硫,提高废气净化效果,同时液体本身对烟尘具有一定的降温效果和滞留效果,提升对废气的过滤效果。Please refer to FIG. 4 , a circulation cavity is excavated in the liquid storage box 10 , and a flow channel connected with the circulation cavity is excavated at the inner end of the magnet ring 9 . A booster pump 8 is installed at one end of the tube 7 away from the liquid storage box 10, a drip hole is drilled at the lower end of the liquid storage box 10, a liquid-adhering hole matching the magnetic suction root 31 is drilled at the inner end of the retention stem 32, and the diverging crown 33 The inner end is drilled with a spherical liquid storage cavity that communicates with the liquid hole, and a plurality of evenly distributed liquid-conducting micro-holes are drilled on the diverging crown 33, which can realize the addition of suitable liquid from the outside according to the characteristics of heavily polluted waste gas, such as waste gas The content of sulfur dioxide in the medium is relatively high, and an appropriate amount of alkaline solution can be added to neutralize the sulfur dioxide in the exhaust gas and improve the purification effect of the exhaust gas.

请继续参阅图1,吸附基环2下侧设有回收平台4,回收平台4内安装有电磁铁5,过滤箱体1内侧壁上开凿有一对竖直且对称分布的升降槽,升降槽内安装有电动滑台6,电动滑台6上的电动滑块与回收平台4之间固定连接,可以收集脱落后的过滤单体3进行集中脱附处理,同时在处理完成后直接送到吸附基环2下侧,利用磁吸作用自动吸附安装完成复位,重新循环利用继续过滤,自脱落式过滤组件的数量可以为多个,不同自脱落式过滤组件的过滤单体3尺寸保持差异,且自上至下尺寸逐渐增大,技术人员可以根据现场待过滤废气的实际情况选择合适的自脱落式过滤组件数量,理论上越多过滤效果越好,但是过滤速度有所下降,应当按照实际情况作出合理调整。Please continue to refer to FIG. 1, a recovery platform 4 is arranged on the lower side of the adsorption base ring 2, an electromagnet 5 is installed in the recovery platform 4, and a pair of vertical and symmetrically distributed lifting grooves are excavated on the inner side wall of the filter box 1. An electric sliding table 6 is installed, and the electric sliding block on the electric sliding table 6 is fixedly connected with the recovery platform 4. The filter unit 3 after falling off can be collected for centralized desorption treatment, and at the same time, it is directly sent to the adsorption base after the treatment is completed. On the lower side of the ring 2, the magnetic attraction is used to automatically absorb and install to complete the reset, and it is recycled to continue filtering. The number of self-dropping filter components can be multiple. The size from top to bottom gradually increases, and the technician can choose the appropriate number of self-detaching filter components according to the actual situation of the exhaust gas to be filtered on site. In theory, the more filtering effect, the better the filtering effect, but the filtering speed is decreased, so it should be reasonable according to the actual situation. Adjustment.

值得注意的是,过滤单体3的具体尺寸应该根据实际的废气污染程度和过滤要求而定,本实施例中不做限定,同时本领域技术人员应当知晓,本发明在低过滤要求的情况下可以直接用于过滤,在高精度过滤要求的情况下,自脱落式过滤组件上方还应安装有现有的精细过滤器,可以显著降低精细过滤器的过滤压力和后续其余净化处理的难度。It is worth noting that the specific size of the filter unit 3 should be determined according to the actual exhaust gas pollution degree and filtration requirements, which is not limited in this embodiment. At the same time, those skilled in the art should know that the present invention is in the case of low filtration requirements. It can be directly used for filtration. In the case of high-precision filtration requirements, an existing fine filter should be installed above the self-detaching filter assembly, which can significantly reduce the filtration pressure of the fine filter and the difficulty of subsequent purification.

本发明可以实现模仿蒲公英的自脱落行为,将现有的过滤网单元化,以类似柔毛的分布形式展开,形成初步的空间过滤网,同时基于活性炭纤维材料的优异吸附性能,在过滤大粒径固体颗粒的同时,主动吸附废气含有的杂质和有害物质,为后续的废气净化降低处理难度,同时其是基于磁力连接的方式起到悬挂作用,待至吸附饱和后重量增大,抵抗磁力后产生脱落行为,不再阻挡废气的流通,配合后续的精细过滤处理实现不停机不降速的预过滤,同时采用润湿液体的方式,提高对废气的净化效果,针对废气特点选用合适的液体,不仅起到对废气的冷却作用,同时通过液体自身的滞留作用和对废气中有害物质的化学反应作用,进一步增加净化效果,同时在脱落后进行脱附处理,方便回收集中处理污染物,且可以重复循环利用,符合可持续发展的环保理念。The invention can realize the self-shedding behavior of imitating the dandelion, unitize the existing filter net, and expand it in a distribution form similar to pilose to form a preliminary space filter net. At the same time, it actively adsorbs the impurities and harmful substances contained in the exhaust gas, which reduces the processing difficulty for the subsequent exhaust gas purification. At the same time, it plays a suspension role based on the magnetic connection. After the adsorption is saturated, the weight increases and resists the magnetic force. It produces shedding behavior, no longer blocks the flow of exhaust gas, and cooperates with subsequent fine filtration treatment to achieve pre-filtration without stopping and slowing down. At the same time, the method of wetting liquid is used to improve the purification effect of exhaust gas. It not only cools the exhaust gas, but also further increases the purification effect through the retention of the liquid itself and the chemical reaction of harmful substances in the exhaust gas. Recycling is in line with the environmental protection concept of sustainable development.

以上所述,仅为本发明较佳的具体实施方式;但本发明的保护范围并不局限于此。任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,根据本发明的技术方案及其改进构思加以等同替换或改变,都应涵盖在本发明的保护范围内。The above description is only a preferred embodiment of the present invention; however, the protection scope of the present invention is not limited thereto. Any person skilled in the art who is familiar with the technical scope of the present invention, according to the technical solution of the present invention and its improvement concept, equivalently replaces or changes, should be covered within the protection scope of the present invention.

Claims (10)

1. The utility model provides a heavily pollute exhaust purification with imitative dandelion from dropping formula filter equipment, includes filter box (1), its characterized in that: the filter box body (1) is provided with a plurality of air inlets distributed in an annular array, the filter box body (1) is internally provided with a self-dropping filter assembly, the self-dropping filter assembly comprises an adsorption base ring (2) and a plurality of filter monomers (3), the filter monomers (3) are uniformly distributed at the lower side of the adsorption base ring (2), the inner side of the adsorption base ring (2) is provided with a plurality of magnet rings (9) distributed in a grid manner, the upper end of each magnet ring (9) is fixedly connected with a liquid storage box (10), a connecting wire (11) is fixedly connected between the adjacent liquid storage boxes (10), the connecting wire (11) at the outer side in the circumferential direction is fixedly connected with the inner end of the adsorption base ring (2), the filter monomers (3) comprise a magnetic attraction root (31), a detention stem part (32) and a diffusion crown part (33) which are sequentially distributed from top to bottom, the diffusion crown part (33) is fixedly connected with a plurality of uniformly distributed filter fluff, and the divergent crown part (33) and the filtering fluff (34) are integrally formed, the outer surface of the divergent crown part (33) is wrapped with the adsorption spherical shell (13), and the outer surface of the filtering fluff (34) is wrapped with the adsorption surface layer (14).
2. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: offer the chisel in stock solution box (10) and have the circulation cavity, magnet ring (9) inner is offered the chisel and is had the runner that is linked together with the circulation cavity, one of them stock solution box (10) upper end is fixed the intercommunication has feed liquor pipe (7), feed liquor pipe (7) are kept away from stock solution box (10) one end and are installed booster pump (8), the chisel has the drip hole stock solution box (10) lower extreme, it has in the same direction as the liquid hole with magnetism absorption root (31) assorted to be offered the chisel in stem (32) inner, it has the spherical stock solution chamber that is linked together with in the same direction as the liquid hole to offer the chisel in diverging crown (33) inner, it has a plurality of evenly distributed's the liquid micropore of leading to offer the chisel on crown (33).
3. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the internal diameter that the internal diameter of magnet ring (9) is greater than magnetism and inhales root (31) is less than the external diameter of magnetism and inhales root (31), magnet ring (9) lower extreme fixedly connected with and magnetism inhale root (31) assorted correction ring (15), and the internal diameter of correction ring (15) slightly is greater than the external diameter of magnetism and inhales root (31).
4. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the magnetic attraction root (31) is made of ferromagnetic metal materials, a nanometer waterproof layer is coated at the lower end of the magnet ring (9), and the magnetic attraction force of the magnet ring (9) on the magnetic attraction root (31) is slightly larger than the gravity of the filtering monomer (3).
5. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the outer end of the retention stem part (32) is provided with a plurality of adsorption micropores (12), and bentonite adsorption layers attached to each other are arranged in the adsorption micropores (12).
6. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the retention stem part (32), the divergent crown part (33) and the filtration fluff (34) are all made of light plastics, the adsorption spherical shell (13) and the adsorption surface layer (14) are all made of activated carbon fiber materials, the diameter of the activated carbon fiber is 5-20 mu m, the specific surface area is 1000-1500m2/g, and the average pore diameter is 1.0-4.0 nm.
7. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the ratio of the radius of the divergent crown (33) to the length of the filtering fluff (34) is 1: 2-8.
8. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the shortest distance between the adjacent pair of the filtering single bodies (3) is just twice of the length of the filtering fluff (34).
9. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: adsorb base ring (2) downside and be equipped with recovery platform (4), install electro-magnet (5) in recovery platform (4), it has the lift groove of a pair of vertical and symmetric distribution to cut on filter box (1) inside wall, install electronic slip table (6) in the lift groove, fixed connection between electronic slider on electronic slip table (6) and recovery platform (4).
10. The dandelion-like self-falling type filtering device for purifying the heavily polluted waste gas as claimed in claim 1, which is characterized in that: the number of the self-dropping type filtering components can be multiple, different sizes of the filtering monomers (3) of the self-dropping type filtering components are different, and the sizes of the filtering monomers are gradually increased from top to bottom.
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CN112604445A (en) * 2020-12-30 2021-04-06 刘露雨 Coal-fired ceramic tunnel kiln flue gas desulfurization denitration dust removal integration equipment
CN113441543A (en) * 2021-06-29 2021-09-28 王群峰 Heavy metal contaminated mine soil remediation device

Citations (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1444357A1 (en) * 1987-01-26 1988-12-15 Ч.-К.А.Будревич Centrifugal gas cleaner
DE4221489A1 (en) * 1992-06-29 1994-01-05 Delbag Luftfilter Gmbh Recyclable air filter - has filter element with magnetic strips for retention in filter frame
US5411709A (en) * 1991-03-25 1995-05-02 Fuji Xerox Co., Ltd. Gas detector
US5824126A (en) * 1996-10-24 1998-10-20 Chen; Cheng Ho Soot filtering cap in a range hood
JPH1133327A (en) * 1997-07-24 1999-02-09 Mitsubishi Denki Bill Techno Service Kk Filter cleaning device
US6238467B1 (en) * 1999-09-24 2001-05-29 Gore Enterprise Holdings, Inc. Rigid multi-functional filter assembly
US20020085183A1 (en) * 2000-12-29 2002-07-04 Han-Ming Wu Purging gas from a photolithography enclosure between a mask protective device and a patterned mask
WO2002085495A1 (en) * 2001-04-19 2002-10-31 Don Korff W G Device for locating and retrieving small articles
US20040103625A1 (en) * 2002-11-29 2004-06-03 Agilent Technologies, Inc. Air blower apparatus for use in inspection apparatus and inspection apparatus housing with the air blower apparatus
WO2004108252A1 (en) * 2003-06-03 2004-12-16 Nikon Corporation Filter apparatus, exposure apparatus, and device-producing method
US20060032378A1 (en) * 2002-03-01 2006-02-16 Ebara Corporation Scrubber and exhaust gas treatment apparatus
EP1675682A2 (en) * 2003-10-24 2006-07-05 Aushon Biosystems, Inc. Apparatus and method for dispensing fluid, semi-solid and solid samples
CN103343859A (en) * 2013-07-30 2013-10-09 台州同盛铜业有限公司 Magnetic dirt remover
CN103670492A (en) * 2013-12-17 2014-03-26 中国矿业大学 Dual-fluid magnetization foam dustfall system and method
CN203598635U (en) * 2013-09-18 2014-05-21 天津市金美化工有限公司 Caustic soda granulated wet dust removal device
CN104310571A (en) * 2014-10-11 2015-01-28 昆明理工大学 Method for purifying poisonous and harmful organic pollutants by using electromagnetic collaborative enhanced biological packed tower
CN104408864A (en) * 2014-11-27 2015-03-11 中国科学技术大学先进技术研究院 Air-suction-type plane cargo compartment fire disaster detector with dehumidifying and dedusting functions
CN104436934A (en) * 2013-09-18 2015-03-25 天津市金美化工有限公司 Sodium hydroxide granulation and wet dust removal apparatus
CN104587766A (en) * 2015-02-04 2015-05-06 青岛路博宏业环保技术开发有限公司 Assembling type filter cartridge deduster
CN204710094U (en) * 2015-06-11 2015-10-21 林文堡 Energy-efficient packed absorber
CN104998510A (en) * 2015-08-11 2015-10-28 东北大学 Removing device and method for inhalable particles and fine particles in flue gas
CN205055237U (en) * 2014-06-04 2016-03-02 自由风股份有限公司 Air that will pass through purification provides air filtration system in enclosure space
CN106178755A (en) * 2016-08-31 2016-12-07 叶青 A kind of hot waste gas environment-friendly temperature-reducing dust removal and filtration system
CN106474838A (en) * 2016-11-18 2017-03-08 广西金邦泰科技有限公司 A kind of steadiness dust protection cloth bag for being provided with vibrating mechanism
CN107159449A (en) * 2017-07-17 2017-09-15 东北大学 The apparatus and method of magnetic-particle in rotating excitation field gas recovery
CN107308743A (en) * 2017-08-18 2017-11-03 马鞍山市顺达环保设备有限公司 A kind of cloth-bag type industrial dedusting equipment
CN108060878A (en) * 2016-12-05 2018-05-22 喻洪根 A kind of self-suction air water filtering type air purification door
CN109718609A (en) * 2018-12-20 2019-05-07 徐菡 A kind of Multifunctional air clarifying device and method
CN110072584A (en) * 2016-10-18 2019-07-30 费雪派克医疗保健有限公司 Valve module and filter
CN110237616A (en) * 2019-07-18 2019-09-17 苏州荣能环保科技有限公司 A kind of quick dust-collecting type dust flue gas environmental protection filter plant

Patent Citations (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU1444357A1 (en) * 1987-01-26 1988-12-15 Ч.-К.А.Будревич Centrifugal gas cleaner
US5411709A (en) * 1991-03-25 1995-05-02 Fuji Xerox Co., Ltd. Gas detector
DE4221489A1 (en) * 1992-06-29 1994-01-05 Delbag Luftfilter Gmbh Recyclable air filter - has filter element with magnetic strips for retention in filter frame
US5824126A (en) * 1996-10-24 1998-10-20 Chen; Cheng Ho Soot filtering cap in a range hood
JPH1133327A (en) * 1997-07-24 1999-02-09 Mitsubishi Denki Bill Techno Service Kk Filter cleaning device
US6238467B1 (en) * 1999-09-24 2001-05-29 Gore Enterprise Holdings, Inc. Rigid multi-functional filter assembly
US20020085183A1 (en) * 2000-12-29 2002-07-04 Han-Ming Wu Purging gas from a photolithography enclosure between a mask protective device and a patterned mask
WO2002085495A1 (en) * 2001-04-19 2002-10-31 Don Korff W G Device for locating and retrieving small articles
US20060032378A1 (en) * 2002-03-01 2006-02-16 Ebara Corporation Scrubber and exhaust gas treatment apparatus
US20040103625A1 (en) * 2002-11-29 2004-06-03 Agilent Technologies, Inc. Air blower apparatus for use in inspection apparatus and inspection apparatus housing with the air blower apparatus
WO2004108252A1 (en) * 2003-06-03 2004-12-16 Nikon Corporation Filter apparatus, exposure apparatus, and device-producing method
EP1675682A2 (en) * 2003-10-24 2006-07-05 Aushon Biosystems, Inc. Apparatus and method for dispensing fluid, semi-solid and solid samples
CN103343859A (en) * 2013-07-30 2013-10-09 台州同盛铜业有限公司 Magnetic dirt remover
CN203598635U (en) * 2013-09-18 2014-05-21 天津市金美化工有限公司 Caustic soda granulated wet dust removal device
CN104436934A (en) * 2013-09-18 2015-03-25 天津市金美化工有限公司 Sodium hydroxide granulation and wet dust removal apparatus
CN103670492A (en) * 2013-12-17 2014-03-26 中国矿业大学 Dual-fluid magnetization foam dustfall system and method
CN205055237U (en) * 2014-06-04 2016-03-02 自由风股份有限公司 Air that will pass through purification provides air filtration system in enclosure space
CN104310571A (en) * 2014-10-11 2015-01-28 昆明理工大学 Method for purifying poisonous and harmful organic pollutants by using electromagnetic collaborative enhanced biological packed tower
CN104408864A (en) * 2014-11-27 2015-03-11 中国科学技术大学先进技术研究院 Air-suction-type plane cargo compartment fire disaster detector with dehumidifying and dedusting functions
CN104587766A (en) * 2015-02-04 2015-05-06 青岛路博宏业环保技术开发有限公司 Assembling type filter cartridge deduster
CN204710094U (en) * 2015-06-11 2015-10-21 林文堡 Energy-efficient packed absorber
CN104998510A (en) * 2015-08-11 2015-10-28 东北大学 Removing device and method for inhalable particles and fine particles in flue gas
CN106178755A (en) * 2016-08-31 2016-12-07 叶青 A kind of hot waste gas environment-friendly temperature-reducing dust removal and filtration system
CN110072584A (en) * 2016-10-18 2019-07-30 费雪派克医疗保健有限公司 Valve module and filter
CN106474838A (en) * 2016-11-18 2017-03-08 广西金邦泰科技有限公司 A kind of steadiness dust protection cloth bag for being provided with vibrating mechanism
CN108060878A (en) * 2016-12-05 2018-05-22 喻洪根 A kind of self-suction air water filtering type air purification door
CN107159449A (en) * 2017-07-17 2017-09-15 东北大学 The apparatus and method of magnetic-particle in rotating excitation field gas recovery
CN107308743A (en) * 2017-08-18 2017-11-03 马鞍山市顺达环保设备有限公司 A kind of cloth-bag type industrial dedusting equipment
CN109718609A (en) * 2018-12-20 2019-05-07 徐菡 A kind of Multifunctional air clarifying device and method
CN110237616A (en) * 2019-07-18 2019-09-17 苏州荣能环保科技有限公司 A kind of quick dust-collecting type dust flue gas environmental protection filter plant

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
王加东: "脉冲布袋除尘器的常见故障及其原因分析", 《环境工程》 *
盛楠: "喷漆废气处理技术研究进展", 《化工进展》 *
郭志强: "汽车涂装车间废气处理系统选型技术要求", 《现代涂装》 *

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* Cited by examiner, † Cited by third party
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CN111495044A (en) * 2020-04-18 2020-08-07 张宏 Unitized self-replacement type efficient waste gas filtering device
CN111514699A (en) * 2020-04-22 2020-08-11 蒋惠良 Anti-blocking adsorption filtering device for waste gas treatment
CN111514699B (en) * 2020-04-22 2021-12-10 内蒙古大唐国际托克托发电有限责任公司 Anti-blocking adsorption filtering device for waste gas treatment
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CN111530226B (en) * 2020-05-08 2021-01-01 黄龙标 Unitized self-cleaning type filtering device for organic waste gas treatment
CN111530226A (en) * 2020-05-08 2020-08-14 黄龙标 A unitized self-cleaning filter device for organic waste gas treatment
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CN111603887A (en) * 2020-06-01 2020-09-01 杭州小鲤工业设计有限公司 Industrial waste gas treatment device and treatment method thereof
CN111540570B (en) * 2020-06-09 2021-10-29 济宁鲁星电气科技有限公司 Transformer cabinet based on self-feedback uniform heat dissipation
CN111540570A (en) * 2020-06-09 2020-08-14 冯国民 Transformer cabinet based on self-feedback uniform heat dissipation
CN111744356A (en) * 2020-06-10 2020-10-09 苏州华烯环保科技有限公司 Waste gas condensation recovery device
CN111841245A (en) * 2020-06-22 2020-10-30 陈利强 Oppression flap is from dropping formula exhaust treatment device
CN111871086A (en) * 2020-07-06 2020-11-03 龙井和 Imitative dandelion formula printing and dyeing waste gas's floccule adsorption equipment
CN111939657A (en) * 2020-07-06 2020-11-17 王迁 Self-cleaning type filter screen of high temperature waste gas of imitative freshwater mussel feed
CN111804142A (en) * 2020-07-09 2020-10-23 江苏融汇环境工程有限公司 Sewage sludge stink waste gas biological hair pendulum type deodorization equipment
CN111804142B (en) * 2020-07-09 2022-06-21 江苏融汇环境工程有限公司 Sewage sludge stink waste gas biological hair pendulum type deodorization equipment
CN111974140A (en) * 2020-07-15 2020-11-24 达小莉 Dandelion seed-imitating oil-containing waste gas following treatment method
CN111790239A (en) * 2020-07-23 2020-10-20 张振娜 Self-compensation type oil-containing waste gas circulating treatment method
CN111905495A (en) * 2020-08-05 2020-11-10 四川淼垚森环保科技有限公司 Dust adsorption treatment system for industrial workshop
CN112604445A (en) * 2020-12-30 2021-04-06 刘露雨 Coal-fired ceramic tunnel kiln flue gas desulfurization denitration dust removal integration equipment
CN113441543A (en) * 2021-06-29 2021-09-28 王群峰 Heavy metal contaminated mine soil remediation device
CN113441543B (en) * 2021-06-29 2022-09-23 青海九零六工程勘察设计院有限责任公司 Heavy metal contaminated mine soil remediation device

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