CN206980422U - Cleaning equipment for waste organic gas - Google Patents
Cleaning equipment for waste organic gas Download PDFInfo
- Publication number
- CN206980422U CN206980422U CN201720777534.4U CN201720777534U CN206980422U CN 206980422 U CN206980422 U CN 206980422U CN 201720777534 U CN201720777534 U CN 201720777534U CN 206980422 U CN206980422 U CN 206980422U
- Authority
- CN
- China
- Prior art keywords
- waste gas
- organic waste
- purifier
- emulsifier
- purification device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002699 waste material Substances 0.000 title description 2
- 238000004140 cleaning Methods 0.000 title 1
- 239000007789 gas Substances 0.000 claims abstract description 84
- 239000010815 organic waste Substances 0.000 claims abstract description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 72
- 238000000746 purification Methods 0.000 claims abstract description 45
- 238000001816 cooling Methods 0.000 claims abstract description 35
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 27
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims description 46
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 30
- 238000001179 sorption measurement Methods 0.000 claims description 25
- 238000009833 condensation Methods 0.000 claims description 18
- 230000005494 condensation Effects 0.000 claims description 18
- 238000004064 recycling Methods 0.000 abstract description 5
- 239000003463 adsorbent Substances 0.000 abstract description 3
- 239000005416 organic matter Substances 0.000 description 13
- 238000004090 dissolution Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- NWGKJDSIEKMTRX-AAZCQSIUSA-N Sorbitan monooleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O NWGKJDSIEKMTRX-AAZCQSIUSA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 231100000331 toxic Toxicity 0.000 description 2
- 230000002588 toxic effect Effects 0.000 description 2
- -1 Octol ethers Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000006552 photochemical reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002503 polyoxyethylene-polyoxypropylene Polymers 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 1
- 235000019801 trisodium phosphate Nutrition 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
本实用新型涉及一种有机废气净化装置,包括进气管、与所述进气管连通的冷却除雾器、与所述冷却除雾器的出气口连通的净化器以及用于生成乳化水的乳化器,所述乳化器连接有高压水泵,所述高压水泵通过高压水管与所述进气管连通。本实用新型装置能够有效净化有机废气,净化过程中的吸附剂可再生,净化回收后的有机废气可以用作一般有机溶剂回收利用,减少二次污染的产生。
The utility model relates to an organic waste gas purification device, which comprises an air intake pipe, a cooling demister communicated with the air intake pipe, a purifier communicated with an air outlet of the cooling demister, and an emulsifier for generating emulsified water , the emulsifier is connected with a high-pressure water pump, and the high-pressure water pump communicates with the air intake pipe through a high-pressure water pipe. The device of the utility model can effectively purify the organic waste gas, the adsorbent in the purification process can be regenerated, and the purified and recovered organic waste gas can be used as a general organic solvent for recycling, thereby reducing the generation of secondary pollution.
Description
技术领域technical field
本实用新型涉及有机废气处理技术领域,具体地说,涉及一种有机废气净化装置。The utility model relates to the technical field of organic waste gas treatment, in particular to an organic waste gas purification device.
背景技术Background technique
随着化学和表面喷涂工业的发展,越来越多的挥发性有机气体作为工业废气排放到大气中,这些有机废气往往带有特殊的气味,其主要污染物组成包括芳香烃、醛类、酮类、卤代烃、醇类等,均属于有毒有害化合物,部分有机废气还具有一定的致癌作用。此外,有机废气在阳光和空气的作用下,会与大气中的氧化剂发生光化学反应,生成毒性更大的光化学烟雾。这些废气对生态环境和人体健康存在很大的潜在危害。因此,有机废气的无害化处理十分重要,可有效保护大气环境。With the development of chemical and surface spraying industries, more and more volatile organic gases are discharged into the atmosphere as industrial waste gases. These organic waste gases often have special odors. The main pollutants include aromatic hydrocarbons, aldehydes, and ketones. Hydrocarbons, halogenated hydrocarbons, alcohols, etc. are all toxic and harmful compounds, and some organic waste gases also have certain carcinogenic effects. In addition, under the action of sunlight and air, organic waste gas will undergo photochemical reactions with oxidants in the atmosphere to generate more toxic photochemical smog. These exhaust gases have great potential harm to the ecological environment and human health. Therefore, the harmless treatment of organic waste gas is very important, which can effectively protect the atmospheric environment.
目前对挥发性工业有机废气常用的处理方法主要有吸附法和燃烧法。吸附法利用吸附剂吸附有机废气,一般适用于处理低浓度有机废气,缺点是吸附剂难以再生,需要不断更换。燃烧法工艺比较简单,操作方便,可回收燃烧后的热量,但不能回收有用物质,只对高浓度有机废气有效,燃烧过程中还易产生二次污染。At present, the commonly used treatment methods for volatile industrial organic waste gas mainly include adsorption method and combustion method. The adsorption method uses an adsorbent to absorb organic waste gas, and is generally suitable for treating low-concentration organic waste gas. The disadvantage is that the adsorbent is difficult to regenerate and needs to be replaced continuously. The combustion process is relatively simple, easy to operate, and can recover the heat after combustion, but cannot recover useful substances. It is only effective for high-concentration organic waste gas, and it is easy to produce secondary pollution during the combustion process.
实用新型内容Utility model content
本实用新型的目的在于针对现有有机废气处理过程中存在的吸附剂难以再生、易产生二次污染等上述问题,提供了一种有机废气净化装置,能够有效净化有机废气,净化过程中的吸附剂可再生,净化后的有机废气可以用作一般有机溶剂回收利用,减少二次污染的产生。The purpose of this utility model is to provide an organic waste gas purification device which can effectively purify organic waste gas, and the adsorption in the purification process The solvent can be regenerated, and the purified organic waste gas can be used as a general organic solvent for recycling to reduce secondary pollution.
为了达到上述目的,本实用新型提供了一种有机废气净化装置,包括进气管、与所述进气管连通的冷却除雾器、与所述冷却除雾器的出气口连通的净化器以及用于生成乳化水的乳化器,所述乳化器连接有高压水泵,所述高压水泵通过高压水管与所述进气管连通。In order to achieve the above object, the utility model provides an organic waste gas purification device, comprising an air intake pipe, a cooling demister connected to the air intake pipe, a purifier connected to the air outlet of the cooling demister, and a An emulsifier for generating emulsified water, the emulsifier is connected with a high-pressure water pump, and the high-pressure water pump communicates with the air intake pipe through a high-pressure water pipe.
进一步的,还包括用于分离乳化水和有机溶剂的破乳化器,所述破乳化器的进液口分别与所述冷却除雾器的出液口和所述净化器的出液口连通,所述破乳化器的出液口与所述乳化器的进液口连通。Further, it also includes a demulsifier for separating emulsified water and organic solvent, the liquid inlet of the demulsifier communicates with the liquid outlet of the cooling demister and the liquid outlet of the purifier respectively, The liquid outlet of the demulsifier communicates with the liquid inlet of the emulsifier.
作为优选,所述冷却除雾器内设有多层冷凝板,每层冷凝板均设有冷却管以及用于液体流通的通孔。Preferably, the cooling demister is provided with multiple layers of condensing plates, and each layer of condensing plates is provided with cooling pipes and through holes for liquid circulation.
作为优选,所述净化器包括净化器本体,所述净化器本体内设有活性炭吸附层,所述净化器本体的顶部设有出气口,所述净化器本体的底部设有与所述破乳化器的进液口连通的出液口,所述净化器本体一侧设有与所述冷却除雾器的出气口连通的进气口。Preferably, the purifier includes a purifier body, an activated carbon adsorption layer is provided in the purifier body, an air outlet is provided on the top of the purifier body, and an The liquid outlet is connected to the liquid inlet of the purifier, and the side of the purifier body is provided with an air inlet connected to the air outlet of the cooling demister.
进一步的,所述活性炭吸附层的下方设有用于支撑活性炭吸附层的挡板,所述挡板上设有多个用于气体流通的通孔。Further, a baffle for supporting the activated carbon adsorption layer is provided under the activated carbon adsorption layer, and a plurality of through holes for gas circulation are provided on the baffle.
进一步的,所述乳化器与所述高压水泵之间连接有过滤器。Further, a filter is connected between the emulsifier and the high-pressure water pump.
与现有技术相比,本实用新型的有益效果在于:Compared with the prior art, the utility model has the beneficial effects of:
(1)本实用新型提供的有机废气净化装置结构简单,操作方便,简化了废气净化结构,占地面积小,有机废气经过冷凝净化与吸附净化二次净化,将有机废气通过与雾化后的乳化水混合,再冷凝后形成冷凝液体,未冷凝的有机废气经过净化器吸附净化,进一步去除有机废气中的有害物质,有效净化有机废气,安全性高。(1) The organic waste gas purification device provided by the utility model is simple in structure, easy to operate, simplifies the waste gas purification structure, and occupies a small area. The organic waste gas is purified twice through condensation purification and adsorption purification. The emulsified water is mixed and condensed to form a condensed liquid. The uncondensed organic waste gas is adsorbed and purified by the purifier to further remove harmful substances in the organic waste gas, effectively purify the organic waste gas, and have high safety.
(2)本实用新型提供的有机废气净化装置还设有破乳化器,冷凝以后形成的液体经破乳化将有机废气中的有机溶剂分离出来回收,而净化有机溶剂的水可以循环利用,无二次污染产生,减少了对水的污染以及废水的产生量。(2) The organic waste gas purification device provided by the utility model is also equipped with a demulsifier, and the liquid formed after condensation is demulsified to separate and recycle the organic solvent in the organic waste gas, and the water for purifying the organic solvent can be recycled without any waste. Secondary pollution, reducing water pollution and waste water production.
附图说明Description of drawings
图1为本实用新型具体实施例有机废气净化装置的结构图。Fig. 1 is a structural diagram of an organic waste gas purification device according to a specific embodiment of the present invention.
图2为本实用新型具体实施有机废气净化装置中冷却除雾器的截面图。Fig. 2 is a cross-sectional view of the cooling demister in the organic waste gas purification device of the utility model.
图中,1、进气管,2、冷却除雾器,21、冷凝板,22、冷却管,23、通孔, 24、出气口,25、出液口,3、净化器,31、活性炭吸附层、32、出气口,33、出液口,34、进气口,35、挡板,4、乳化器,41、进液口,5、高压水泵,51、高压水管,6、破乳化器,61、第一进液口,62、第二进液口,63、第一出液口, 64、第一控制阀,65、第二控制阀,66、第三控制阀,67、第二出液口,68、第四控制阀,7、过滤器。In the figure, 1. Intake pipe, 2. Cooling demister, 21. Condenser plate, 22. Cooling pipe, 23. Through hole, 24. Air outlet, 25. Liquid outlet, 3. Purifier, 31. Activated carbon adsorption Layer, 32, air outlet, 33, liquid outlet, 34, air inlet, 35, baffle, 4, emulsifier, 41, liquid inlet, 5, high-pressure water pump, 51, high-pressure water pipe, 6, demulsifier , 61, the first liquid inlet, 62, the second liquid inlet, 63, the first liquid outlet, 64, the first control valve, 65, the second control valve, 66, the third control valve, 67, the second Liquid outlet, 68, the fourth control valve, 7, filter.
具体实施方式detailed description
下面,通过示例性的实施方式对本实用新型进行具体描述。然而应当理解,在没有进一步叙述的情况下,一个实施方式中的元件、结构和特征也可以有益地结合到其他实施方式中。Below, the utility model is described in detail through exemplary embodiments. It should be understood, however, that elements, structures and characteristics of one embodiment may be beneficially incorporated in other embodiments without further recitation.
在本实用新型的描述中,需要说明的是,术语“内”、“顶”、“底”、“一侧”、“下”等指示的方位或位置关系为基于附图所示的位置关系,仅是为了便于描述本实用新型和简化描述,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实用新型的限制。此外,术语“第一”、“第二”、“第三”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 utility model, it should be noted that the orientation or positional relationship indicated by the terms "inner", "top", "bottom", "side", "lower" etc. is based on the positional relationship shown in the drawings , is only for the convenience of describing the utility model and simplifying the description, but does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be construed as a limitation of the utility model. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.
参见图1,本实用新型实施例提供了一种有机废气净化装置,包括进气管1、与所述进气管1连通的冷却除雾器2、与所述冷却除雾器2的出气口连通的净化器3以及用于生成乳化水的乳化器4,所述乳化器4连接有高压水泵5,所述高压水泵5通过高压水管51与所述进气管1连通。Referring to Fig. 1, an embodiment of the present utility model provides an organic waste gas purification device, including an air intake pipe 1, a cooling demister 2 connected to the air intake pipe 1, and a cooling demister 2 connected to the air outlet of the cooling demister 2 The purifier 3 and the emulsifier 4 for generating emulsified water, the emulsifier 4 is connected with a high-pressure water pump 5 , and the high-pressure water pump 5 communicates with the air intake pipe 1 through a high-pressure water pipe 51 .
本实用新型提供的有机废气净化装置,设有冷却除雾器、净化器和乳化器,乳化器中的乳化水通过高压水泵形成雾化的水汽与有机废气混合,提高有机废气在水汽中的溶解扩散速率和溶解量,提高吸附能力及净化能力。有机废气净化过程中,乳化水汽与有机废气结合进入冷却除雾器进行冷凝,冷凝下来的液体沉降,未冷凝的有机废气进入净化器进一步吸附净化,有机废气经过冷凝净化与吸附净化二次净化,能够有效净化有机废气,安全性高。The organic waste gas purification device provided by the utility model is equipped with a cooling demister, a purifier and an emulsifier. The emulsified water in the emulsifier is mixed with the organic waste gas to form atomized water vapor through a high-pressure water pump, so as to improve the dissolution of the organic waste gas in the water vapor. Diffusion rate and dissolution rate, improve adsorption capacity and purification capacity. During the purification process of organic waste gas, the emulsified water vapor and organic waste gas are combined into the cooling demister for condensation, the condensed liquid settles, and the uncondensed organic waste gas enters the purifier for further adsorption and purification, and the organic waste gas undergoes secondary purification through condensation purification and adsorption purification. It can effectively purify organic waste gas and has high safety.
继续参见图1,为了防止净化过程中产生二次污染,对上述有机废气净化装置进一步设计,所述有机废气净化装置还包括用于分离乳化水和有机溶剂的破乳化器6,所述破乳化器6的第一进液口61与所述冷却除雾器2的出液口25,所述破乳化器6的第二进液口62与所述净化器3的出液口33连通,所述破乳化器6的出液口63与所述乳化器4的进液口41连通。冷却除雾器中冷凝沉降的液体进入破乳化器中进行破乳化,使有机物与破乳化水进行分离,上层为有机溶剂可以进行回收并重新使用,下层为破乳化水可以在流入乳化器内,再次乳化,重复利用,利用率高,节约了运行处理成本,用水量少,且不产生二次污染。Continue to refer to Fig. 1, in order to prevent secondary pollution during the purification process, the above-mentioned organic waste gas purification device is further designed, and the organic waste gas purification device also includes a demulsifier 6 for separating emulsified water and organic solvent, and the demulsification The first liquid inlet 61 of the device 6 communicates with the liquid outlet 25 of the cooling demister 2, and the second liquid inlet 62 of the demulsifier 6 communicates with the liquid outlet 33 of the purifier 3, so The liquid outlet 63 of the demulsifier 6 communicates with the liquid inlet 41 of the emulsifier 4 . The liquid condensed and settled in the cooling demister enters the demulsifier for demulsification, so that the organic matter is separated from the demulsified water. The upper layer is the organic solvent that can be recycled and reused, and the lower layer is the demulsified water that can flow into the emulsifier. Re-emulsification, repeated use, high utilization rate, saving operation and treatment costs, less water consumption, and no secondary pollution.
继续参见图1,作为上述有机废气净化装置进一步设计,为了便于控制凝结后含有有机物的水进入破乳化器进行破乳化,在破乳化器6的第一进液口61处设有第一控制阀64、第二进液口62处设有第二控制阀65,通过两个控制阀控制进入破乳化器中的含有有机物的水。同时,为了便于控制破乳化后的破乳化水进入乳化器循环利用,在破乳化器6的第一出液口63处设有第三控制阀66,通过第三控制阀66控制破乳化后的水进入乳化器4循环利用。Continuing to refer to Fig. 1, as a further design of the above-mentioned organic waste gas purification device, in order to facilitate the control of the condensed water containing organic matter entering the demulsifier for demulsification, a first control valve is provided at the first liquid inlet 61 of the demulsifier 6 64. The second liquid inlet 62 is provided with a second control valve 65, and the water containing organic matter entering the demulsifier is controlled through two control valves. At the same time, in order to facilitate the control of demulsified demulsified water entering the emulsifier for recycling, the first liquid outlet 63 of the demulsifier 6 is provided with a third control valve 66, through which the demulsified demulsified water is controlled. Water enters the emulsifier 4 for recycling.
继续参见图1,作为上述有机废气净化装置进一步设计,为了便于回收破乳化器中破乳化后分离出来的有机溶剂,所述破乳化器6上还设有用于有机溶剂流出的第二出液口67,为了便于控制有机溶剂的流出,在所述第二出液口67处还设有第四控制阀68。Continue to refer to Figure 1, as the above-mentioned organic waste gas purification device is further designed, in order to facilitate the recovery of the organic solvent separated after demulsification in the demulsifier, the demulsifier 6 is also provided with a second liquid outlet for the organic solvent to flow out 67. In order to facilitate the control of the outflow of the organic solvent, a fourth control valve 68 is also provided at the second liquid outlet 67.
为了提高冷却除雾器的冷凝效果,作为上述有机废气净化装置优选设计,所述冷却除雾器内设有多层冷凝板,每层冷凝板均设有冷却管以及用于液体流通的通孔。继续参见图1,并参见图2,在上述有机废气净化装置的一优选设计中,所述冷却除雾器2内设有5层冷凝板21,每层冷凝板均设有冷却管22以及用于液体流通的通孔23,所述冷却管22位于所述冷凝版21下方。应当说明的是,冷凝板的层数不限于5层,可以根据有机废气的进气量进行调整,可以是4 层、6层、7层、8层不等。为了提高冷凝效果,冷凝板的层数越多越有利于水汽的凝结。In order to improve the condensation effect of the cooling demister, as the preferred design of the above-mentioned organic waste gas purification device, the cooling demister is equipped with multi-layer condensation plates, and each layer of condensation plates is provided with cooling pipes and through holes for liquid circulation . Continue to refer to Fig. 1, and refer to Fig. 2, in a preferred design of the above-mentioned organic waste gas purification device, the cooling demister 2 is provided with five layers of condensation plates 21, and each layer of condensation plates is provided with cooling pipes 22 and The cooling pipe 22 is located below the condensation plate 21 through the through hole 23 through which the liquid circulates. It should be noted that the number of layers of the condensing plate is not limited to 5 layers, and can be adjusted according to the intake volume of organic waste gas, and can be 4 layers, 6 layers, 7 layers, or 8 layers. In order to improve the condensation effect, the more layers of condensation plates, the more conducive to the condensation of water vapor.
继续参见图1,作为上述有机废气净化装置优选设计,所述净化器3包括净化器本体,所述净化器本体内设有活性炭吸附层31,所述净化器本体的顶部设有出气口32,所述净化器本体的底部设有与所述破乳化器6的第二进液口62连通的出液口33,所述净化器本体一侧设有与所述冷却除雾器2的出气口24连通的进气口34。经冷却除雾器冷凝净化后的未冷凝的有机废气进入净化器中,通过活性炭吸附层的吸附进一步吸收有机废气中的有害物质,实现有机废气的二次净化,有机废气在净化器中净化过程中凝结的液体进入破乳化器中破乳化,回收有机溶剂和破乳化水,循环利用,通过净化器净化后的有机废气通过出气口排除即可,无二次污染产生。Continuing to refer to Fig. 1, as the preferred design of the above-mentioned organic waste gas purification device, the purifier 3 includes a purifier body, an activated carbon adsorption layer 31 is arranged in the purifier body, and an air outlet 32 is provided on the top of the purifier body, The bottom of the purifier body is provided with a liquid outlet 33 communicating with the second liquid inlet 62 of the demulsifier 6, and one side of the purifier body is provided with an air outlet connected to the cooling demister 2 24 connected to the air inlet 34 . The uncondensed organic waste gas condensed and purified by the cooling demister enters the purifier, and the harmful substances in the organic waste gas are further absorbed through the adsorption of the activated carbon adsorption layer, so as to realize the secondary purification of the organic waste gas. The organic waste gas is purified in the purifier. The condensed liquid enters the demulsifier for demulsification, recovers the organic solvent and demulsified water for recycling, and the organic waste gas purified by the purifier can be discharged through the gas outlet without secondary pollution.
继续参见图1,由于活性炭吸附层由活性炭颗粒组成,为了防止其掉落,堵塞出液口,作为优选设计,所述活性炭吸附层31的下方设有用于支撑活性炭吸附层的挡板35,通过挡板支撑活性炭吸附层。为了使有机废气顺利进入活性炭吸附层,所述挡板35上设有多个用于气体流通的通孔(未示出)。Continue to refer to Fig. 1, because the activated carbon adsorption layer is made up of activated carbon particles, in order to prevent it from falling, block the liquid outlet, as a preferred design, the bottom of the activated carbon adsorption layer 31 is provided with a baffle plate 35 for supporting the activated carbon adsorption layer, through The baffle supports the activated carbon adsorption layer. In order to allow the organic waste gas to enter the activated carbon adsorption layer smoothly, the baffle plate 35 is provided with a plurality of through holes (not shown) for gas circulation.
继续参见图1,为了防止乳化水中含有的杂质堵塞高压水泵,影响高压水泵的正常工作,作为上述有机废气净化装置进一步设计,在所述乳化器5与所述高压水泵5之间连接有过滤器7,乳化器中的乳化水进入高压水泵之前通过过滤器先进行过滤,滤出乳化水中的杂质。Continue to refer to Fig. 1, in order to prevent the impurities contained in the emulsified water from clogging the high-pressure water pump and affecting the normal operation of the high-pressure water pump, as the above-mentioned organic waste gas purification device is further designed, a filter is connected between the emulsifier 5 and the high-pressure water pump 5 7. The emulsified water in the emulsifier is filtered through a filter before entering the high-pressure water pump to filter out impurities in the emulsified water.
采用上述实施例所述的有机废气净化装置进行有机废气处理,其具体步骤为:Using the organic waste gas purification device described in the above embodiments to treat organic waste gas, the specific steps are:
S1:在乳化器中加入水,并加入乳化剂充分搅拌溶解,形成具有乳化能力的乳化水;S1: Add water to the emulsifier, and add emulsifier to fully stir and dissolve to form emulsified water with emulsifying ability;
S2:通过高压水泵对乳化水进行加压汽化,使乳化水形成雾化液滴;S2: The emulsified water is pressurized and vaporized by a high-pressure water pump, so that the emulsified water forms atomized droplets;
S3:有机废气在进气管内与高压水管中的雾化液滴在高压气流中充分接触混合形成含有有机物的过饱和水汽;S3: The organic waste gas in the intake pipe and the atomized liquid droplets in the high-pressure water pipe are fully contacted and mixed in the high-pressure airflow to form supersaturated water vapor containing organic matter;
S4:过饱和水汽进入冷却除雾器冷凝后形成水滴沉降;S4: The supersaturated water vapor enters the cooling demister and condenses to form water droplet settlement;
S5:未沉降的气体进入净化器,经净化器净化处理后获得净化后的气体。S5: The unsettled gas enters the purifier, and the purified gas is obtained after being purified by the purifier.
本实用新型提供的上述有机废气净化装置进行有机废气处理时,通过高压水泵加压汽化乳化水形成雾化的水汽与有机废气混合,提高有机废气在水汽中的溶解扩散速率和溶解量,提高吸附能力及净化能力。乳化水汽与有机废气结合进入冷却除雾器进行冷凝,冷凝下来的液体沉降,未冷凝的有机废气进入净化器进一步吸附净化,有机废气经过冷凝净化与吸附净化二次净化,能够有效净化有机废气,安全性高。When the above-mentioned organic waste gas purification device provided by the utility model is used for organic waste gas treatment, the vaporized emulsified water is pressurized by a high-pressure water pump to form atomized water vapor and mixed with organic waste gas, so as to improve the dissolution diffusion rate and dissolved amount of organic waste gas in water vapor, and improve adsorption. ability and purification ability. The emulsified water vapor and organic waste gas are combined into the cooling demister for condensation, the condensed liquid settles, and the uncondensed organic waste gas enters the purifier for further adsorption and purification. The organic waste gas is purified by condensation purification and adsorption purification for the second time, which can effectively purify the organic waste gas. High security.
作为进一步设计,步骤S4中,冷却除雾器中沉降下来的含有有机物的水进入破乳化器中,当吸附的有机物与水开始分层时,在破乳化器中加入破乳剂进行破乳化,使有机物与破乳化的水充分分离,回收分离后的有机物,分离后的破乳化的水进入乳化器中继续使用。As a further design, in step S4, the water containing organic matter settled in the cooling demister enters in the demulsifier, and when the adsorbed organic matter and water start to separate, add a demulsifier in the demulsifier for demulsification, so that The organic matter is fully separated from the demulsified water, the separated organic matter is recovered, and the separated demulsified water enters the emulsifier for further use.
在一优选实施例中,为了加速含有有机物的水中的有机溶剂与乳化水的分离,所述破乳化器中,在含有有机物的水加入浓度为0.1%-3%的聚氧乙烯聚氧丙烯十八醇醚作为破乳剂。为了能够使冷凝沉降后的含有有机物的水中的有机溶剂与乳化水有效进行分离,本实用新型对破乳剂的浓度进行了限定。可以理解的是,本领域的技术人员可以根据实际情况选择上述范围内的浓度进行合理加入。In a preferred embodiment, in order to accelerate the separation of the organic solvent in the water containing organic matter and the emulsified water, in the demulsifier, a concentration of 0.1%-3% of polyoxyethylene polyoxypropylene decoction is added to the water containing organic matter Octol ethers act as demulsifiers. In order to effectively separate the organic solvent and the emulsified water in the water containing organic matter after condensation and sedimentation, the utility model limits the concentration of the demulsifier. It can be understood that those skilled in the art can select the concentration within the above range for reasonable addition according to the actual situation.
在一优选实施例中,所述乳化器中,乳化剂由浓度为1%-5%的十二烷基苯磺酸钠、浓度为0.1%-2%的Span-80和浓度为1%-5%的磷酸三钠组成。为了能够有效提高水对有机组分的乳化和亲和能力,提高有机废气在水汽中的溶解扩散速率和溶解量,本实用新型对乳化剂的组成及含量进行了限定。可以理解的是,本领域的技术人员可以根据实际情况选择上述范围内的配比进行合理加入。In a preferred embodiment, in the emulsifier, the emulsifier is composed of sodium dodecylbenzenesulfonate with a concentration of 1%-5%, Span-80 with a concentration of 0.1%-2%, and Span-80 with a concentration of 1%- 5% trisodium phosphate composition. In order to effectively improve the emulsification and affinity of water to organic components, and increase the dissolution rate and amount of organic waste gas dissolved in water vapor, the utility model limits the composition and content of the emulsifier. It can be understood that those skilled in the art can select the proportion within the above range for reasonable addition according to the actual situation.
为了更清楚详细的介绍本实用新型实施例所提供的有机废气净化装置下面将结合具体实施例进行描述。In order to introduce the organic waste gas purification device provided by the embodiment of the present utility model more clearly and in detail, the following will be described in conjunction with specific embodiments.
实施例1:某表面涂装厂对有机废气只是高空排放,污染周围环境,采用本实用新型上述有机废气净化装置对有机废气回收和净化后,有机物回收率达到 99%,排放的废气浓度达到地方标准。Example 1: A surface coating factory only discharges organic waste gas at high altitudes, polluting the surrounding environment. After the above-mentioned organic waste gas purification device of the utility model is used to recycle and purify the organic waste gas, the recovery rate of organic matter reaches 99%, and the concentration of the discharged waste gas reaches local standard.
实施例2:某喷漆厂未对有机废气进行处理,只是简单抽气排放,排放不达标。采用本实用新型上述有机废气净化装置对有机废气回收和净化后,有机物回收率达到99%,排放的废气浓度达到地方标准,不再污染环境。Example 2: A painting factory did not treat the organic waste gas, but simply pumped and discharged it, and the discharge did not meet the standard. After adopting the above-mentioned organic waste gas purifying device of the utility model to recycle and purify the organic waste gas, the recovery rate of organic matter reaches 99%, the concentration of the discharged waste gas reaches the local standard, and the environment is no longer polluted.
上述实施例用来解释本实用新型,而不是对本实用新型进行限制,在本实用新型的精神和权利要求的保护范围内,对本实用新型做出的任何修改和改变,都落入本实用新型的保护范围。The above-described embodiments are used to explain the utility model, rather than to limit the utility model. Within the spirit of the utility model and the scope of protection of the claims, any modifications and changes made to the utility model all fall into the scope of the utility model. protected range.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720777534.4U CN206980422U (en) | 2017-06-29 | 2017-06-29 | Cleaning equipment for waste organic gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720777534.4U CN206980422U (en) | 2017-06-29 | 2017-06-29 | Cleaning equipment for waste organic gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206980422U true CN206980422U (en) | 2018-02-09 |
Family
ID=61400114
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720777534.4U Expired - Fee Related CN206980422U (en) | 2017-06-29 | 2017-06-29 | Cleaning equipment for waste organic gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206980422U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107115766A (en) * | 2017-06-29 | 2017-09-01 | 东营市胜利第中学 | Cleaning equipment for waste organic gas and method |
CN115475487A (en) * | 2022-09-11 | 2022-12-16 | 昆明理工大学 | System and method for absorbing organic matters in waste tire waste gas through pyrolysis |
-
2017
- 2017-06-29 CN CN201720777534.4U patent/CN206980422U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107115766A (en) * | 2017-06-29 | 2017-09-01 | 东营市胜利第中学 | Cleaning equipment for waste organic gas and method |
CN115475487A (en) * | 2022-09-11 | 2022-12-16 | 昆明理工大学 | System and method for absorbing organic matters in waste tire waste gas through pyrolysis |
CN115475487B (en) * | 2022-09-11 | 2024-01-16 | 昆明理工大学 | System and method for absorbing organic matters in waste gas generated by pyrolysis of waste tires |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2020237990A1 (en) | Industrial waste gas treatment device | |
KR20060054307A (en) | Multiphase separation system | |
WO2013060244A1 (en) | Active coke regeneration mixed vapor treatment method and apparatus | |
CN105289217B (en) | VOCs recycling systems in a kind of waste gas | |
CN107497278A (en) | Horizontal exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
CN106938173A (en) | A kind of micro-nano bubble dyeing waste-water of plasma, VOCs coprocessing systems | |
CN207641271U (en) | Vertical exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
KR20150128589A (en) | Antifoam device and method of use for seawater foam control | |
CN206980422U (en) | Cleaning equipment for waste organic gas | |
CN103252155B (en) | Device for treating organic waste gas with oil-in-water emulsion and method for treating organic waste gas | |
WO2015169125A1 (en) | Method for removing dust in gas fumes | |
CN206103392U (en) | Humid tropical vapor recovery system and purifier | |
CN104436946A (en) | Environment-friendly processing system for coating workshop | |
CN205598839U (en) | Exhaust gas purification system suitable for laboratory | |
KR101364097B1 (en) | Apparatus for treatment exhaunst gas containing VOC | |
CN104289072A (en) | Cascade recovery apparatus and method for benzene hydrocarbon volatile gases | |
CN109455845B (en) | Method and device for co-processing waste gas and waste water of steam maintenance plant | |
CN111617613B (en) | A method and system for treating waste gas in a refining and chemical enterprise | |
CN207871896U (en) | A kind of intermediate pollution equipment for treating industrial waste gas | |
CN101810987A (en) | Resource tail gas treatment system and technology for soil vapor extraction repair technique | |
CN206473964U (en) | A kind of VOCs processing units | |
CN107115766A (en) | Cleaning equipment for waste organic gas and method | |
CN108722104A (en) | A kind of device of efficient process uncontrollable discharge VOCs | |
CN207805361U (en) | Horizontal exhaust treatment system based on dynamic interception and micro-nano bubbler techniques | |
CN203916422U (en) | A kind of oil-poor device for recovering oil and gas |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180209 Termination date: 20190629 |