CN111408233A - Gas treatment device - Google Patents
Gas treatment device Download PDFInfo
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- CN111408233A CN111408233A CN202010367361.5A CN202010367361A CN111408233A CN 111408233 A CN111408233 A CN 111408233A CN 202010367361 A CN202010367361 A CN 202010367361A CN 111408233 A CN111408233 A CN 111408233A
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- 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
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/0036—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions by adsorption or absorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/74—Regeneration of the filtering material or filter elements inside the filter by forces created by movement of the filter element
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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
- B01D53/04—Separation 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
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
- B01D53/502—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound characterised by a specific solution or suspension
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
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- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/60—Simultaneously removing sulfur oxides and nitrogen oxides
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
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- B01D—SEPARATION
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- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
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- B01D2251/304—Alkali metal compounds of sodium
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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Abstract
Description
技术领域technical field
本发明涉及气体处理净化技术领域,特别涉及一种气体处理装置。The present invention relates to the technical field of gas treatment and purification, in particular to a gas treatment device.
背景技术Background technique
伴随社会工业的发展,工厂废气、汽车尾气等对大气的影响日趋严重,因此,各国对环保的重视程度不断提升,对各类废气、尾气的排放要求不断提高;无论是工厂或餐饮行业的废气,还是汽车尾气,均需要首先对排放的含有有害物质的气体进行处理,达到一定指标要求后,才准予排放到大气中。在一些对空气洁净度要求较高的特定行业或环境,还需要对空气进行更高要求的净化处理,才能满足使用的要求。因此,气体处理净化技术被深入研发并广泛应用。With the development of social industry, the impact of factory exhaust gas and automobile exhaust gas on the atmosphere is becoming more and more serious. Therefore, countries are paying more and more attention to environmental protection, and the emission requirements for various types of exhaust gas and exhaust gas are constantly increasing; whether it is exhaust gas from factories or catering industries , or vehicle exhaust, it is necessary to first process the discharged gas containing harmful substances, and only after meeting certain index requirements can it be discharged into the atmosphere. In some specific industries or environments that require higher air cleanliness, it is also necessary to purify the air with higher requirements to meet the requirements of use. Therefore, gas treatment purification technology has been deeply developed and widely used.
在现有的气体处理设备中,仍主要基于过滤装置,如滤网、滤芯、过滤棉等对经过的气体进行拦截过滤,或是通过水液的喷淋进行除尘。喷淋除尘需要耗费大量的水、且产生较多的污水;采用过滤装置则需要定期冲洗或更换滤材,滤材耗费造成装置的运行成本偏高。In the existing gas treatment equipment, it is still mainly based on filtering devices, such as filter screens, filter elements, filter cotton, etc., to intercept and filter the passing gas, or to remove dust by spraying with water. Spray dust removal requires a lot of water and generates a lot of sewage; if a filter device is used, it is necessary to regularly flush or replace the filter material, and the consumption of filter material results in a high operating cost of the device.
发明内容SUMMARY OF THE INVENTION
有鉴于此,本发明旨在提出一种气体处理装置,以延长气体处理装置中的滤材寿命,从而降低气体处理净化的成本。In view of this, the present invention aims to provide a gas treatment device, so as to prolong the life of the filter material in the gas treatment device, thereby reducing the cost of gas treatment and purification.
为达到上述目的,本发明的技术方案是这样实现的:In order to achieve the above object, the technical scheme of the present invention is achieved in this way:
一种气体处理装置,具有由壳体围构形成的空腔、以及设置于所述空腔内的过滤单元,所述壳体的两端分设有供气体进出所述空腔的入气口和排气口,所述过滤单元被驱动旋转地设置于所述入气口和所述排气口之间;所述空腔内盛装有处理液,以构成所述过滤单元部分地浸入于所述处理液中;于所述处理液的液面上方,形成供所述气体流经的通道;所述气体于流经途中,穿越附带有所述处理液的所述过滤单元。A gas processing device has a cavity formed by a casing, and a filter unit arranged in the cavity, the two ends of the casing are respectively provided with an air inlet and a discharge port for gas to enter and exit the cavity an air port, the filter unit is driven and rotated between the air inlet and the exhaust port; the cavity is filled with a treatment liquid, so that the filter unit is partially immersed in the treatment liquid in the middle; above the liquid level of the treatment liquid, a channel for the gas to flow through is formed; the gas passes through the filter unit with the treatment liquid on the way.
进一步的,所述过滤单元为回转体,于所述过滤单元所在处的所述空腔具有供所述过滤单元于所述空腔内密封转动的空间。Further, the filter unit is a rotary body, and the cavity where the filter unit is located has a space for the filter unit to be sealed and rotated in the cavity.
进一步的,处理液的液面位于过滤单元高度的三分之一至三分之二之间。Further, the liquid level of the treatment liquid is located between one third and two thirds of the height of the filter unit.
进一步的,过滤单元包括边框,以及若干层布设于边框之中、呈薄壁状的过滤体。Further, the filter unit includes a frame, and several layers of thin-walled filter bodies arranged in the frame.
进一步的,过滤单元布设有一层过滤体,过滤体呈迎着气体的流向凸起的曲面状。Further, the filter unit is provided with a layer of filter body, and the filter body is in the shape of a convex curved surface facing the flow direction of the gas.
进一步的,过滤单元上间隔地布设有多层过滤体,并于各过滤体之间填充有可作用于气体的填料。Further, multiple layers of filter bodies are arranged on the filter unit at intervals, and fillers that can act on the gas are filled between the filter bodies.
进一步的,所述过滤体为多孔过滤结构体或吸附体。Further, the filter body is a porous filter structure body or an adsorbent body.
进一步的,沿气体的流向,于空腔内顺次地间隔设置有多个过滤单元,且各过滤单元上的过滤体的孔隙顺次地由大到小。Further, along the flow direction of the gas, a plurality of filter units are arranged at intervals in the cavity in sequence, and the pores of the filter body on each filter unit are sequentially from large to small.
进一步的,壳体的底部构造有与空腔连通、并逆着气体的流向下倾的沉降槽;由处理液捕捉或反应生成的沉降物经沉降槽滑移至沉降槽的末端,并可经开设于末端的排泄口排出。Further, the bottom of the shell is constructed with a settling tank that communicates with the cavity and slopes downward against the flow of the gas; the sediment captured or reacted by the treatment liquid slides to the end of the settling tank through the settling tank, and can pass through the settling tank. The discharge port opened at the end is discharged.
进一步的,壳体的上部开设有填充口,且于壳体上设有可对空腔内的处理液构成监测的液位检测装置;处理液可因应空腔内的液面变化由填充口适量补入,而可构成空腔内液位的保持。Further, the upper part of the casing is provided with a filling port, and a liquid level detection device that can monitor the treatment liquid in the cavity is arranged on the casing; the treatment liquid can be adjusted by the filling port according to the change of the liquid level in the cavity. Fill in, and can constitute the maintenance of the liquid level in the cavity.
相对于现有技术,本发明具有以下优势:Compared with the prior art, the present invention has the following advantages:
(1)本发明所述的气体处理装置,在壳体内的空腔中盛装部分的处理液,过滤单元被部分浸泡并旋转地安装在壳体内;气体流经过滤单元时,气体中的粉尘可因过滤单元的拦截和处理液的附着而被去除,气体中的有害气体也可被适配的处理液反应或溶解吸收;被拦截的粉尘或吸收的物质还可被冲刷入处理液而离开过滤单元;使得气体处理装置不仅具备较好的气体处理效果,且过滤单元中的滤材因及时的冲洗而寿命延长,从而有利于气体处理净化成本的节降。(1) In the gas treatment device of the present invention, a part of the treatment liquid is contained in the cavity in the casing, and the filter unit is partially soaked and installed in the casing in a rotating manner; when the gas flows through the filter unit, the dust in the gas can be removed. Due to the interception of the filter unit and the adhesion of the treatment liquid, the harmful gas in the gas can also be reacted or dissolved and absorbed by the appropriate treatment liquid; the intercepted dust or absorbed substances can also be washed into the treatment liquid and leave the filter The gas treatment device not only has a better gas treatment effect, but also the filter material in the filter unit has a longer life due to timely flushing, which is conducive to reducing the cost of gas treatment and purification.
(2)空腔和过滤单元采用回转体状,利于过滤单元的旋转布置,可使过滤单元很好地将空腔分隔开来,从而为气体的流通过滤创造良好的条件。(2) The cavity and the filter unit are in the shape of a revolving body, which is conducive to the rotating arrangement of the filter unit, and the filter unit can well separate the cavity, thereby creating good conditions for the flow and filtration of the gas.
(3)处理液的液面保持在过滤单元的轴线以上,可确保对过滤单元的全部浸湿。(3) The liquid level of the treatment liquid is maintained above the axis of the filter unit, so that the entire wetting of the filter unit can be ensured.
(4)采用一或两层的过滤体过滤,即可达到预定的过滤效果,也利于过滤体在边框上的安装及过滤体的冲刷。(4) Using one or two layers of filter body for filtration can achieve the predetermined filtering effect, which is also conducive to the installation of the filter body on the frame and the scouring of the filter body.
(5)采用曲面结构的过滤体,可借助离心力将附着在过滤体上的固态杂质甩出,有助于过滤体的清洁。(5) The filter body with curved surface structure can use centrifugal force to throw out the solid impurities attached to the filter body, which is helpful for the cleaning of the filter body.
(6)采用两层过滤体,并加装活性炭等特定的填料,可对气体中的特定成分起到反应或吸收的效果,从而增强气体处理装置的处理性能。(6) The use of two layers of filters and the addition of specific fillers such as activated carbon can react or absorb specific components in the gas, thereby enhancing the treatment performance of the gas treatment device.
(7)采用滤网,便于配备,且具备适合冲刷清洁、耐用性高等特点。(7) The filter screen is used, which is easy to be equipped, and has the characteristics of being suitable for scouring cleaning and high durability.
(8)顺次设置多个过滤单元,可根据气体中有害物质的成分、粉尘粒径的大小等不同情况,有针对性的设置各种滤除功能的过滤单元,从而提升气体处理装置的气体处理性能和适用性。(8) Multiple filter units are set up in sequence. According to different conditions such as the composition of harmful substances in the gas and the size of the dust particle size, filter units with various filtering functions can be set up in a targeted manner, so as to improve the gas quality of the gas treatment device. Handling performance and suitability.
(9)在壳体底部构造沉降槽,可积存并滑出处理液中悬浮或反应生成并慢慢沉降的固态物质,从而改善处理液的清澈度。(9) A settling tank is constructed at the bottom of the shell, which can accumulate and slide out the solid substances suspended or reacted in the treatment liquid and slowly settle, thereby improving the clarity of the treatment liquid.
(10)在壳体上加设液位检测装置,当排泄口排出固态物质时带走液体从而造成空腔内液位下降时,可通过填充口实时补入空腔,从而保持处理液的液面高度,并为处理液的置换或循环使用创造良好条件;有利于装置处理性能的保持。(10) A liquid level detection device is installed on the shell. When the solid material is discharged from the discharge port, the liquid is taken away and the liquid level in the cavity drops, which can be filled into the cavity in real time through the filling port, so as to maintain the liquid level of the treatment liquid. Surface height, and create good conditions for the replacement or recycling of the treatment liquid; it is conducive to the maintenance of the treatment performance of the device.
附图说明Description of drawings
构成本发明的一部分的附图,是用来提供对本发明的进一步理解,本发明的示意性实施例及其说明是用于解释本发明,其中涉及到的前后、上下等方位词语仅用于表示相对的位置关系,均不构成对本发明的不当限定。在附图中:The accompanying drawings that form a part of the present invention are used to provide a further understanding of the present invention, the schematic embodiments of the present invention and their descriptions are used to explain the present invention, and the azimuth words such as front and rear, upper and lower, etc. involved are only used to indicate The relative positional relationship does not constitute an improper limitation of the present invention. In the attached image:
图1为本发明实施例一所述的气体处理装置的整体结构示意图;FIG. 1 is a schematic diagram of the overall structure of the gas processing device according to
图2为本发明实施例一所述的气体处理装置于另一视角下的整体结构示意图;2 is a schematic diagram of the overall structure of the gas processing device according to
图3为本发明实施例一所述气体处理装置的内部结构示意图;3 is a schematic diagram of the internal structure of the gas processing device according to
图4为图1中A-A所示部位的剖面结构示意图;Fig. 4 is the sectional structure schematic diagram of the position shown in A-A in Fig. 1;
图5为图4中B所示部位的局部放大图;Fig. 5 is a partial enlarged view of the part shown in B in Fig. 4;
图6为本发明实施例二所述的气体处理装置的剖面结构示意;6 is a schematic cross-sectional structure diagram of the gas processing device according to the second embodiment of the present invention;
附图标记说明:Description of reference numbers:
1-壳体,100-下壳体,101-入气端侧板,102-排气端侧板,103-沉降槽,104-封装翻边,105-紧固螺栓,106-入气口,1061-挡水罩,107-补气孔,108-排气口,109-隔仓板,110-上壳体,120-填充口,121-第一填充口,122-第二填充口,130-积废仓,131-第一积废仓,132-第二积废仓,133-第一排泄口,134-第二排泄口,135-积废腔,136-封堵部件,137-回液孔,138-回液口,140-容料筐,141-第一容料筐,142-第二容料筐,143-填料盒,1430-料腔,1431-承托翻边,1432-避让部,1433-通孔,144-透孔,150-喷头;1- Shell, 100- Lower shell, 101- Air inlet side plate, 102- Discharge end side plate, 103- Settlement tank, 104- Encapsulation flange, 105- Fastening bolt, 106- Air inlet, 1061 -Water retaining cover, 107- Air supply hole, 108- Exhaust port, 109- Compartment plate, 110- Upper shell, 120- Filling port, 121- First filling port, 122- Second filling port, 130- Volume Waste bin, 131-first waste bin, 132-second waste bin, 133-first discharge port, 134-second discharge port, 135-waste chamber, 136-blocking member, 137-liquid return hole , 138- liquid return port, 140- container, 141- first container, 142- second container, 143- stuffing box, 1430- cavity, 1431- supporting flange, 1432- avoidance part , 1433-through hole, 144-through hole, 150-spray head;
2-过滤单元,200-过滤体,201-边框,202-支撑架,203-转轴,204-电机,205-轴承,206-轴封,207-密封体,21-第一过滤单元,22-第二过滤单元,23-第三过滤单元,24-第四过滤单元。2-filter unit, 200-filter body, 201-frame, 202-support frame, 203-rotating shaft, 204-motor, 205-bearing, 206-shaft seal, 207-seal body, 21-first filter unit, 22- The second filter unit, 23 - the third filter unit, 24 - the fourth filter unit.
具体实施方式Detailed ways
需要说明的是,在不冲突的情况下,本发明中的实施例及实施例中的特征可以相互组合。It should be noted that the embodiments of the present invention and the features of the embodiments may be combined with each other under the condition of no conflict.
此外,在本发明的描述中,涉及到的左、右、上、下等方位名词,是为了描述方便而基于图示状态下的用语,不应理解为构成对本发明结构的限定;提到的第一、第二、第三等也均是为了便于描述,而不能理解为指示或暗示相对的重要性。In addition, in the description of the present invention, the directional nouns such as left, right, upper and lower involved are for the convenience of description and are based on the terms in the illustrated state, and should not be construed as constituting a limitation to the structure of the present invention; the mentioned The first, second, third, etc. are also for the convenience of description and should not be construed as indicating or implying relative importance.
实施例一Example 1
本实施例涉及一种气体处理装置,可以延长气体处理装置中的滤材寿命,从而降低气体处理净化的成本。该气体处理装置,具有由壳体围构形成的空腔、以及设置于所述空腔内的过滤单元,所述壳体的两端分设有供气体进出所述空腔的入气口和排气口,所述过滤单元被驱动旋转地分隔于所述入气口和所述排气口之间;所述空腔内未满地盛装有处理液,所述过滤单元部分地冲刷于所述处理液中;于所述处理液的液面上方,形成供所述气体流经的通道;所述气体于流经途中,穿越浸湿有所述处理液的所述过滤单元;因所述过滤单元的拦截和/或所述处理液的作用,而构成对所述气体内有害物质的去除分离。This embodiment relates to a gas treatment device, which can prolong the life of the filter material in the gas treatment device, thereby reducing the cost of gas treatment and purification. The gas processing device has a cavity formed by a casing, and a filter unit arranged in the cavity. The two ends of the casing are respectively provided with an air inlet and an exhaust for gas to enter and exit the cavity. The filter unit is driven and rotated to be separated between the air inlet and the exhaust port; the cavity is not filled with treatment liquid, and the filter unit is partially flushed with the treatment liquid above the liquid level of the treatment liquid, a channel for the gas to flow through is formed; the gas passes through the filter unit soaked with the treatment liquid during the flow; The interception and/or the action of the treatment liquid constitutes the removal and separation of harmful substances in the gas.
基于上述的总体结构原则,下面将参考附图并结合实施例来详细说明。本实施例的气体处理装置的一种示例性结构如图1所示,其主要包括壳体1和过滤单元2。Based on the above-mentioned general structural principles, the following will be described in detail with reference to the accompanying drawings and in conjunction with the embodiments. An exemplary structure of the gas treatment device of this embodiment is shown in FIG. 1 , which mainly includes a
结合图2、图3所示,一种优选的结构为:将壳体1分别构造为下壳体100和上壳体110,壳体1的两端的入气端侧板101和排气端侧板102可和下壳体100一体构造。通过壳体1上方的敞口将过滤单元2等部件装配入壳体1的空腔后,再将上壳体110封盖上,通过下壳体100和上壳体110的封装翻边104密封配合,由紧固螺栓105紧固,形成密闭的空腔。Referring to FIG. 2 and FIG. 3 , a preferred structure is as follows: the
空腔的入气口106可设置在入气端侧板101上,排气口108可设在排气端侧板102上,显然,至少排气口108需要靠近壳体1的上部开设,以防止空腔盛装处理液后,处理液淹没排气口108。过滤单元2被设置在空腔内,将入气口106和排气口108分隔开来,其过滤单元2采用可旋转的装配结构,可由外力驱动旋转。如图3和图4所示,可将过滤单元2固装在转轴203上,转轴203的一端或两端穿设在壳体1上,其中一端穿过壳体1的侧壁外露于壳体1外部,在该端加装电机204,由电机204驱动过滤单元2在空腔内旋转。优选地,在转轴203贯穿壳体1侧壁的部位装配轴承205和轴封206,在转轴203的其他枢转固定部位也加装轴承205,以改善转轴203在空腔内的转动稳定性。The
为达到处理液对气体的良好处理效果,并伴随过滤单元2的旋转,利于处理液对过滤单元2形成冲刷,以去除过滤单元2上附着的污染物,在空腔内盛装有处理液;需要说明的是,空腔内的处理液并不能加满,以使过滤单元2可以部分地浸泡在处理液中,并随过滤单元2旋转形成对过滤单元2的冲刷,同时,在处理液的液面上方,可以形成供气体流经的通道即可。当气体在流经途中,会穿越浸湿有处理液的过滤单元2;由于过滤单元2的拦截过滤,气体中的粉尘会被处理;气体中含有的气态的有害物质,如二氧化硫,可通过配置能与二氧化硫反应的碱性的处理液,其他性质的有害气体也可相应配置对应的处理液,达到针对性处理的效果;这样,这些有害物质会被处理液溶解、吸收或反应生成不溶于水的固态沉降物。从而达到气体处理装置去除气体内各类有害物质的效果。结合图4所示,可在入气口106的内侧加装挡水罩1061,防止处理液波动或飞溅时液体倒灌到入气口106的供气管路;排气口108处同样可设置阻挡处理液飞溅出空腔的遮罩结构。优选的,挡水罩1061采用弧形板罩设在入气口106的入口上,挡水罩1061的上下固定在入气端侧板101内壁上,挡水罩1061的左右两侧敞口供气体进入空腔内。In order to achieve the good treatment effect of the treatment liquid on the gas, and along with the rotation of the filter unit 2, it is beneficial for the treatment liquid to scour the filter unit 2 to remove the pollutants attached to the filter unit 2, and the cavity is filled with the treatment liquid; It is explained that the treatment liquid in the cavity cannot be filled up, so that the filter unit 2 can be partially immersed in the treatment liquid, and the filter unit 2 can be washed with the rotation of the filter unit 2. Above the surface, a channel for the gas to flow through can be formed. When the gas flows through, it will pass through the filter unit 2 soaked with the treatment liquid; due to the interception and filtration of the filter unit 2, the dust in the gas will be treated; the gaseous harmful substances contained in the gas, such as sulfur dioxide, can be configured Alkaline treatment liquid that can react with sulfur dioxide and other harmful gases can also be equipped with corresponding treatment liquid to achieve the effect of targeted treatment; in this way, these harmful substances will be dissolved, absorbed or reacted by the treatment liquid to form insoluble in water of solid sediments. So as to achieve the effect of removing various harmful substances in the gas by the gas treatment device. 4, a
仍如图3和图4所示,对于壳体1和过滤单元2的结构形状,可灵活设计,优选地,壳体1的外部以便于装置的固定为原则,壳体1内的过滤单元2采用回转体形状,为保证其良好的旋转运行,于过滤单元2所在处的空腔具有供所述过滤单元2于空腔内密封转动的空间;为了便于构造,空腔优选为圆柱体形状,当然,除了供过滤单元2旋转的空间部分,空腔及其壳体1其他部分的形状可以根据需要构造为各种形状。至少与过滤单元2的外周面相配合的空腔的内壁呈与过滤单元2同轴线的圆柱面。例如,将空腔的内壁设置为圆筒状,或将空腔直接设置为圆柱状,过滤单元2则设计为与空腔同轴线的盘状的回转体。空腔和过滤单元2采用回转体状,利于过滤单元2的旋转布置,可使过滤单元2很好地将空腔分隔开来,从而为气体的流通过滤创造良好的条件。Still as shown in FIG. 3 and FIG. 4 , the structural shapes of the
需要指出的是,可以在空腔的中部加设隔仓板109,形成对转轴203的枢转承托;转轴203贯穿隔仓板109,在隔仓板109的贯穿的轴孔中配装轴承205。同时,还可利用隔仓板109将空腔分隔为两个仓室,或加装多个隔仓板109以分隔出多个仓室,各仓室的上部连通,形成供气体流经的通道;各仓室内盛装不同性质的处理液,且每个仓室均配有一个或多个过滤单元2,以实现对气体内粉尘、多种性质有害气态物质等若干种物质的去除和/或分离。例如,可以将粉尘分离到处理液中,利用可匹配反应的处理液将氮氧化物、二氧化硫等气态物质溶解并反应、以去除它们。It should be pointed out that a
关于空腔内处理液的液面高度,可设置为过滤单元2高度的三一之一到三分之二之间。优选将处理液的液面保持在过滤单元2的轴线之上,这样可确保处理液对过滤单元2的全部浸湿。Regarding the liquid level height of the treatment liquid in the cavity, it can be set between one third and two thirds of the height of the filter unit 2 . It is preferable to keep the liquid level of the treatment liquid above the axis of the filter unit 2 , so as to ensure complete wetting of the filter unit 2 by the treatment liquid.
而为了达到良好的过滤效果,本实施例中,将过滤单元2设计为圆盘状的形式,过滤单元2包括边框201,以及若干层布设于边框201之中、呈薄壁状的过滤体200。采用一或几层的过滤体200过滤,即可达到预定的过滤效果,也利于过滤体200在边框201上的安装及过滤体200的冲刷。In order to achieve a good filtering effect, in this embodiment, the filter unit 2 is designed in the form of a disc. The filter unit 2 includes a
当采用布设一层过滤体200的结构时,过滤体200可以为平面形状,也可以为凸面形,优选地,过滤体200呈迎着气体的流向凸起的曲面状。采用曲面结构的过滤体200,可借助离心力将附着在过滤体200上的固态杂质甩出,有助于过滤体200的清洁。如图4并图5所示,对于过滤单元2的具体结构,为加强其稳固性,可在过滤单元2的固定在转轴203上的中心部件和边框201之间加装支撑架202;其中边框201可设计为圆筒状,被过滤体200甩出的处理液或固态物体被边框201阻挡收集,并随其进入处理液中;当然,也可将过滤体200安装在边框201的气体流向的上游一侧,使被过滤体200甩出的处理液或固态物体被直接甩入处理液中。为保持过滤单元2两侧的相对隔绝效果,可在边框201的外部加装软性耐磨的密封体207,以形成边框201和壳体1的内壁之间的一定密封性,例如可以采用耐磨橡胶制备的胶圈,或密集的毛刷或高密封性轴承等。同时,可以在边框201的两侧或下游一侧、在空腔内壁上构造承托边框201的凸台,以增加过滤单元2受气流冲击时的稳定性。在空腔的内壁面上设有分置于各过滤单元2两侧的环状凸起,并于环状凸起和过滤单元2间设多个滚动件。具体结构上,在环状凸起的朝向对应过滤单元2的侧面上设有支架,滚动件为定位安装在支架上的滚珠。在外边框上设有供滚珠滑动的滑道。此处,通过设置环状凸起和滚动件,可增大壳体1对过滤单元2的承载力,同时,采用滚动摩擦增加了稳固性,并有效减少过滤单元2在旋转过程中的摩擦力,进而减少使用过程中的磨损。When adopting the structure of arranging one layer of
如图4所示,当过滤单元2采用两层过滤体200时,两过滤体200在过滤单元2上间隔布置,并可在两过滤体200之间填充可作用于气体的填料。采用两层过滤体200,并加装活性炭等特定的填料,可对气体中的特定成分起到反应或吸收的效果,从而增强气体处理装置的处理性能。此外,还可在排气口108的下游设置活性炭吸附装置,进一步改善装置的排出气体的洁净度。As shown in FIG. 4 , when the filter unit 2 adopts two layers of
对于过滤体200的材料,可以是过滤滤布、滤网,或使用为多孔过滤结构体或吸附体,例如由活性炭或过滤石材制成的过滤圆盘等。当同一个过滤单元2中有多层的过滤体200时,各个过滤体200可采用同一种滤材,也可采用多种滤材的组合。采用滤网时,可以是金属网、塑料纤维网等,可视气体中含有的污染物情况灵活选用;网的过滤精细度,即网的目数规格,可根据气体的处理需求配备。过滤体200采用滤网时,便于配备,且具备适合冲刷清洁、耐用性高等特点。过滤体200采用为活性碳过滤盘时,由于活性炭在水中同样具备良好的吸附效应,可以吸收气体中的二氧化硫等多种气体,这些被吸附的物质可因处理液的冲刷而溶解于处理液中、或与处理液反应中和,从而起到清洁恢复活性碳性能的效果。而且,在本实施例的应用场景中,克服了活性炭现有应用方式中的诸多问题。例如,现有活性炭在气流中应用由于没有液体的湿润,当气流温度过高可能会引起活性炭的燃烧;活性炭静态浸泡在水中时,由于没有活性炭圆盘在处理液中的旋转冲刷,使用一段时间后,活性炭会吸附较多的杂质,而缺乏必要的清洗,活性炭的性能会很快下降,需要更换。而在本实施例的应用中,克服了上述问题,使活性炭可发挥持久的良好吸附性能。The material of the
同时,在空腔内,沿气体的流向,可顺次地间隔设置多个过滤单元2,且各过滤单元2上的滤网的目数顺次增加,当是其他材质的过滤体200时,其分布的孔隙顺次由大变小。这样,可根据气体中有害物质的成分、粉尘粒径的大小、以及要求达到的气体处理效果等不同情况,有针对性的设置各种滤除功能的过滤单元2,实现逐级的过滤和处理,从而提升气体处理装置的气体处理性能和适用性。At the same time, in the cavity, along the flow direction of the gas, a plurality of filter units 2 can be arranged at intervals in sequence, and the mesh number of the filter screen on each filter unit 2 increases sequentially. When it is a
此外,还可在空腔内布置若干容料筐140,对应容料筐140,在上壳体110上正对的开设多个填充口120,容料筐140可容许转轴203贯穿,容料筐140的侧壁上加工密集的透孔144。通过填充口120除可补充处理液外,还可加装溶解速度较慢的块状填料到容料筐140中,如方解石、石灰石、碳酸钠等,伴随填料的逐渐溶解和反应,可改善处理液的化学处理性能,从而延长装置的处理性能。例如,采用碳酸钙填料时,其在有二氧化碳和水情况下可生成易溶于水的碳酸氢钙,可加速对处理液因吸收二氧化硫等酸性气体后的中和。容料筐140可单独设置,也可对应过滤单元2配对设置,在本实施例中,如图4所示,设有第一过滤单元21和第二过滤单元22,对应第一过滤单元21设有第一容料筐141和第一填充口121,对应第二过滤单元22设有第二容料筐142和第二填充口122。In addition, a plurality of
基于上述的结构,为进一步改善处理液的工作效能,如图4所示,壳体1的底部构造有与空腔连通、并逆着气体的流向下倾的沉降槽103;由处理液捕捉或反应生成的沉降物经沉降槽103滑移至沉降槽103的末端,并可经开设于末端的排泄口排出。在壳体1底部构造沉降槽103,可积存并滑出处理液中悬浮或反应生成并慢慢沉降的固态物质,从而改善处理液的清澈度。本实施例中,在排泄口下方还配设有积废仓130,其包括与第一过滤单元21对应的第一排泄口133下方的第一积废仓131,和与第二过滤单元22对应的第二排泄口134下方的第二积废仓132。它们分别收集对应仓室内沉降并由沉降槽103滑出的固态废料。Based on the above structure, in order to further improve the working efficiency of the treatment liquid, as shown in FIG. 4 , the bottom of the
此外,在通过填充口120补入处理液时,须借助在壳体1上设置的对空腔内的处理液构成监测的液位检测装置,实时了解液位情况,可采用透明的视镜窗口人为查看和控制补液量,也可采用液位计、控制表和补液泵通过简单的连锁控制补液,实现空腔内液面位置的保持。在壳体1上加设液位检测装置,当排泄口排出固态物质时带走液体从而造成空腔内液位下降时,可通过填充口120实时补入空腔,从而保持处理液的液面高度,并为处理液的置换或循环使用创造良好条件;有利于装置处理性能的保持。同时,还可在空腔中设置压力、温度、PH等检测装置,以根据过滤单元2两侧的差压值判断其阻塞情况,实时掌握空腔内的工况温度和处理液的情况。In addition, when replenishing the treatment liquid through the filling
实施例二Embodiment 2
本实施例所述的气体处理装置的另一种结构形式的剖面结构如图6所示,该装置的壳体1内为一个单独仓室的空腔,沿气体的流向依次设置有第一过滤单元21、第二过滤单元22、第三过滤单元23、第四过滤单元24四个过滤单元2,四个过滤单元2的过滤等级依次提升,如筛孔尺寸可由5目递增至40目;或使用不同的滤材,对应去除相应的有害物质。The cross-sectional structure of another structural form of the gas treatment device described in this embodiment is shown in FIG. 6 , the
在第一过滤单元21的上游侧的上方可加装喷头150,实现的气体的初步喷淋除尘,对于气体含有需要补入氧气才容易和处理液反应的气体,可在入气端侧板101上加设补气孔107用于补入空气。上壳体110上可只开设一个填充口120,优选地,填充口120开设在最靠近气体流向的下游位置,这样添加处理液时,处理液的液流可辅助辅助冲走沉降槽103内积存的沉降物。在第一排泄口133的下方设置有积废仓130,积废仓130的底部优选采用锥形,最下端设置排放口,排放口可用封堵部件136封堵,封堵部件136可以是阀门或丝堵等。当沉降物在积废仓130中积存较多时,可开启封堵部件136,固态的废料会夹杂着处理液顺锥面的内壁从排放口排出。A
同时,积废仓130的内腔可分隔为两部分,作为积废仓130主体腔室的积废腔135承接从第一排泄口133下落的沉降物废料;避开第一排泄口133的下方,在积废仓130上部分隔出供处理液排出的小腔,小腔与积废腔135之间开设有回液孔137供处理液流通,在积废仓130的外部设置有与小腔连通的回液口138。当需要对处理液进行排放时可由回液口138排放,也可再回液口138和填充口120之间加装供给泵、反应池等单元,将使用过的处理液经处理后再补回到空腔中,实现处理液的循环使用。At the same time, the inner cavity of the
本实施例的气体处理装置的其他部分可参照实施例一的内容设置,在此不再赘述。The other parts of the gas processing device in this embodiment can be set with reference to the content of the first embodiment, and are not repeated here.
上述各实施例所述的气体处理装置,在壳体1内的空腔中盛装部分的处理液,过滤单元2被部分浸泡并旋转地安装在壳体1内;气体流经过滤单元2时,气体中的粉尘可因过滤单元2的拦截和处理液的附着而被去除,气体中的有害气体也可被适配的处理液反应或溶解吸收;被拦截的粉尘或吸收的物质还可被冲刷入处理液而离开过滤单元2;使得气体处理装置不仅具备较好的气体处理效果,且过滤单元2中的滤材因及时的冲洗而寿命延长,从而有利于气体处理净化成本的节降。In the gas treatment device described in the above-mentioned embodiments, a part of the treatment liquid is contained in the cavity in the
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the scope of the present invention. within the scope of protection.
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