CN207024927U - Industrial VOC waste gas catalytic combustion treatment system - Google Patents
Industrial VOC waste gas catalytic combustion treatment system Download PDFInfo
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- CN207024927U CN207024927U CN201720387240.0U CN201720387240U CN207024927U CN 207024927 U CN207024927 U CN 207024927U CN 201720387240 U CN201720387240 U CN 201720387240U CN 207024927 U CN207024927 U CN 207024927U
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Abstract
Description
【技术领域】【Technical field】
本实用新型涉及一种废气处理装置,特别一种是工业VOC废气催化燃烧处理系统。The utility model relates to a waste gas treatment device, in particular to an industrial VOC waste gas catalytic combustion treatment system.
【背景技术】【Background technique】
烘干窑炉可以用于对工件表面的油漆及涂料进行加热干燥处理。工件在高温处理的过程中,工件中的挥发性有机化合物(VOC)气体随尾气直接排出到环境中,将会对环境造成严重污染,同时会对该区域内的工作人员及居民造成身体损伤。The drying kiln can be used to heat and dry the paint and coating on the surface of the workpiece. During the high-temperature treatment of the workpiece, the volatile organic compound (VOC) gas in the workpiece is directly discharged into the environment along with the exhaust gas, which will cause serious pollution to the environment and cause physical damage to the staff and residents in the area.
目前行业内主要采用冷凝法、吸附-真空脱附后吸收法、燃烧法、膜分离等治理手段,现有有机废气处理手段单一,构造复杂,要么处理效果很差,要么需要消耗大部分能源,提高处理成本。At present, the industry mainly adopts condensation method, adsorption-vacuum desorption post-absorption method, combustion method, membrane separation and other treatment methods. The existing organic waste gas treatment methods are single and complex in structure. Either the treatment effect is poor, or most of the energy is consumed. Increase processing costs.
【实用新型内容】【Content of utility model】
本实用新型的目的是针对上述现技术存在的不足,提供一种可以极大程度消除挥发性有机化合物(VOC)气体排放污染,结构简单、节能高效且更为环保的工业VOC废气催化燃烧处理系统。The purpose of this utility model is to address the shortcomings of the above-mentioned existing technologies, and to provide a catalytic combustion treatment system for industrial VOC waste gas that can greatly eliminate volatile organic compound (VOC) gas emission pollution, has a simple structure, energy saving, high efficiency, and is more environmentally friendly .
为了实现上述目的,本实用新型是这样实现的:工业VOC废气催化燃烧处理系统,包括喷淋处理模块、干燥模块和催化燃烧器,废气排出管与所述喷淋处理模块连接,所述喷淋处理模块与所述干燥模块的干燥通道连接,所述干燥模块与所述催化燃烧器连接,所述催化燃烧器的排放烟气管与排放总管连接,所述排放总管设置有一分支管路与所述干燥模块的热源接口连接。In order to achieve the above object, the utility model is achieved in this way: the industrial VOC waste gas catalytic combustion treatment system includes a spray treatment module, a drying module and a catalytic burner, the exhaust gas discharge pipe is connected with the spray treatment module, and the spray treatment module The processing module is connected to the drying channel of the drying module, the drying module is connected to the catalytic burner, the exhaust gas pipe of the catalytic burner is connected to the discharge main pipe, and the discharge main pipe is provided with a branch pipeline connected to the The heat source interface connection of the drying module described above.
所述喷淋处理模块包括一个处理塔,在所述处理塔内设置下至上依次设有至少一个加湿处理腔和二次除尘腔,所述加湿处理腔和二次除尘腔之间设有过滤填料层相隔;在所述二次除尘腔内设置第一喷淋装置,所述第一喷淋装置安装于所述二次除尘腔的上方;所述处理塔设置有烟气进口和出气口,所述烟气 进口连通所述加湿处理腔,所述出气口连通所述二次除尘腔,在所述加湿处理腔上设置有第二喷淋装置,所述处理塔底端设置处理液池,所述第二喷淋装置通过输送管经水泵与所述处理液池连接。The spray treatment module includes a treatment tower, and at least one humidification treatment chamber and a secondary dust removal chamber are arranged in sequence from bottom to top in the treatment tower, and a filter filler is arranged between the humidification treatment chamber and the secondary dust removal chamber Layers are separated; a first spray device is set in the secondary dust removal chamber, and the first spray device is installed above the secondary dust removal chamber; the treatment tower is provided with a flue gas inlet and a gas outlet, so The flue gas inlet is connected to the humidification treatment chamber, the gas outlet is connected to the secondary dust removal chamber, a second spray device is arranged on the humidification treatment chamber, and a treatment liquid pool is arranged at the bottom of the treatment tower. The second spraying device is connected to the treatment liquid pool through a delivery pipe through a water pump.
所述第一喷淋装置或第二喷淋装置包括设置所述二次除尘腔或加湿处理腔内的螺旋盘管,在所述螺旋盘管上设置有若干喷淋头,可以使烟气与处理液喷雾进行有效接触,最大限度地除去烟气中的硫化物和氮氧化物。The first spraying device or the second spraying device includes a spiral coil pipe arranged in the secondary dust removal chamber or humidification treatment chamber, and several spray heads are arranged on the spiral coil pipe, which can make the flue gas and The treatment liquid is sprayed for effective contact to remove sulfide and nitrogen oxides in the flue gas to the greatest extent.
所述加湿处理腔为分级设置,所述加湿处理腔内通过辅助过滤填料层分割成最少两个子加湿处理腔;一级子加湿处理腔和二级子加湿处理腔内分别设置所述喷淋装置。The humidification treatment chamber is arranged in stages, and the humidification treatment chamber is divided into at least two sub-humidification treatment chambers through the auxiliary filter packing layer; .
与现有技术相比,本实用新型具有的优点和有益技术效果如下:将含有VOC气体的高温烟气全部通过喷淋处理模块进行脱硫及除去大的颗粒物,减少烟气粉尘排放;先将喷淋处理后的废气用回收利用的烟气干燥后进入催化燃烧器进行燃烧分解,可以减轻催化燃烧器处理负担,提高燃烧效果;充分的回收利用燃烧室排放热量,节能效果明显,且VOC完全被燃烧降解,对环境不再造成污染。Compared with the prior art, the utility model has the advantages and beneficial technical effects as follows: all the high-temperature flue gas containing VOC gas is desulfurized and removes large particles through the spray treatment module, reducing the emission of flue gas dust; The exhaust gas after leaching treatment is dried with the recycled flue gas and then enters the catalytic burner for combustion and decomposition, which can reduce the processing burden of the catalytic burner and improve the combustion effect; fully recover and utilize the heat emitted by the combustion chamber, the energy saving effect is obvious, and VOC is completely eliminated Combustion degradation, no pollution to the environment.
【附图说明】【Description of drawings】
图1为本实用新型工业VOC废气催化燃烧处理系统的系统流程图;Fig. 1 is the system flowchart of industrial VOC waste gas catalytic combustion treatment system of the present utility model;
图2为本实用新型工业VOC废气催化燃烧处理系统中喷淋处理模块的结构示意图。Fig. 2 is a schematic structural diagram of the spray treatment module in the industrial VOC waste gas catalytic combustion treatment system of the present invention.
【具体实施方式】【detailed description】
以下结合附图和具体实施例对本实用新型进行详细的描述说明。The utility model is described in detail below in conjunction with the accompanying drawings and specific embodiments.
工业VOC废气催化燃烧处理系统,如图1所示,包括喷淋处理模块2、干燥模块7和催化燃烧器6,家具等喷涂车间的废气排出管1与所述喷淋处理模块2连接,用于处理可能存在的硫化物和去除大颗粒物;所述喷淋处理模块2与所述干燥模块7的干燥通道连接,用于对喷淋处理后的废气进行干燥处理,减轻催化燃烧器处理负担,提高燃烧效果。所述干燥模块7与所述催化燃烧器6连接,所述催化燃烧器6的排放烟气管与排放总管连接,所述排放总管设置有一分支管路与所述干燥模块7的热源接口连接。所述所述干燥 模块7与所述催化燃烧器6连接管道之间设置调节阀门。所述排放总管上设置烟气分配箱14,所述分支管路与所述烟气分配箱14连接。The industrial VOC waste gas catalytic combustion treatment system, as shown in Figure 1, includes a spray treatment module 2, a drying module 7 and a catalytic burner 6, and the exhaust gas discharge pipe 1 of the spraying workshop such as furniture is connected with the spray treatment module 2. It is used to treat possible sulfides and remove large particles; the spray treatment module 2 is connected to the drying channel of the drying module 7, and is used to dry the exhaust gas after the spray treatment, so as to reduce the processing burden of the catalytic burner, Improve combustion effect. The drying module 7 is connected to the catalytic burner 6 , the flue gas exhaust pipe of the catalytic burner 6 is connected to the discharge main pipe, and the discharge main pipe is provided with a branch pipeline connected to the heat source interface of the drying module 7 . A regulating valve is set between the drying module 7 and the connecting pipeline of the catalytic burner 6. A smoke distribution box 14 is arranged on the discharge main pipe, and the branch pipeline is connected with the smoke distribution box 14 .
所述催化燃烧器可以是光催化燃烧器,可以直接购买市场上销售的成熟产品,其主要是利用光催化剂二氧化钛(TiO2)吸收外界辐射的光能,使其直接转变为化学能。对臭氧难以氧化的某些有机物如三氯甲烷、四氯化炭、六氯苯、都能有效地加以分解,所以对难以降解的有机物具有特别意义,光催化的有效氧化剂是羟基自由基(HO),羟基自由基(HO)的氧化性高于常见的臭氧、双氧水、高锰酸钾、次氯酸等。The catalytic burner can be a photocatalytic burner, and can directly purchase a mature product sold in the market, which mainly utilizes the photocatalyst titanium dioxide (TiO2) to absorb the light energy of external radiation and convert it directly into chemical energy. Some organic substances that are difficult to be oxidized by ozone, such as chloroform, carbon tetrachloride, and hexachlorobenzene, can be effectively decomposed, so it has special significance for organic substances that are difficult to degrade. The effective oxidant for photocatalysis is hydroxyl radicals (HO ), the oxidation of hydroxyl radicals (HO) is higher than that of common ozone, hydrogen peroxide, potassium permanganate, hypochlorous acid, etc.
所述干燥模块7为换热器,其包括干燥通道和换热通道,所述干燥通道与所述喷淋处理模块2的出口连接,所述换热通道与所述分支管路连接,用于回收排放余热来对废气进行干燥,节能,且效果明显。The drying module 7 is a heat exchanger, which includes a drying channel and a heat exchange channel, the drying channel is connected to the outlet of the spray treatment module 2, and the heat exchange channel is connected to the branch pipeline for Recycling exhaust waste heat to dry exhaust gas, energy saving, and the effect is obvious.
所述喷淋处理模块,如图2所示,其包括一个处理塔,在所述处理塔内从下至上依次设有至少一个加湿处理腔11和二次除尘腔12,所述加湿处理腔11和二次除尘腔12之间设有过滤填料层13相隔;在所述二次除尘腔12内设置第一喷淋装置53,所述第一喷淋装置53安装于所述二次除尘腔12的上方;第一喷淋装置53包括设置所述二次除尘腔的螺旋盘管,在所述螺旋盘管上设置有若干喷淋头,所述第一喷淋装置53通过输送管和第一水泵52与储水池51连接;所述处理塔靠近底部侧壁设置烟气进口与废气排出管1连接,底部设置排水口16,上部顶端设置出气口,所述烟气进口连通所述加湿处理腔11,所述出气口连通所述二次除尘腔。所述处理塔底端设置有处理液池41,用于收集从所述排水口16流下的处理液。所述排水口16可以置于所述处理液池41内液面以下,这样可以避免烟气溢流。所述加湿处理腔11上部设置有第二喷淋装置43,所述第二喷淋装置43通过输送管经第二水泵42与所述处理液池41连接,循环利用处理液池41内的处理液对从烟气进口进入的烟气进行喷淋水浴处理,有效的去除烟气中的硫化物以及活泼的氮氧化物。所述喷淋装置43包括设置加湿处理腔11内螺旋盘管,在所述螺旋盘管上设置若干喷淋头,可以使烟气与处理液喷雾进行有效接触,最大限度地除去烟气中的硫化物和氮氧化物。The spray treatment module, as shown in Figure 2, includes a treatment tower, in which at least one humidification treatment chamber 11 and a secondary dedusting chamber 12 are sequentially arranged from bottom to top in the treatment tower, and the humidification treatment chamber 11 There is a filter packing layer 13 between the secondary dust removal chamber 12; a first spray device 53 is arranged in the secondary dust removal chamber 12, and the first spray device 53 is installed in the secondary dust removal chamber 12 above; the first spraying device 53 includes a spiral coil tube with the secondary dust removal chamber, and several shower heads are arranged on the spiral coil tube, and the first spraying device 53 passes through the conveying pipe and the first The water pump 52 is connected to the water storage tank 51; the side wall of the treatment tower is provided with a flue gas inlet near the bottom to connect with the exhaust gas discharge pipe 1, the bottom is provided with a drain port 16, and the top of the upper part is provided with an air outlet, and the flue gas inlet is connected to the humidification treatment chamber 11. The air outlet communicates with the secondary dust removal chamber. A treatment liquid pool 41 is provided at the bottom of the treatment tower for collecting the treatment liquid flowing down from the water outlet 16 . The drain port 16 can be placed below the liquid level in the treatment liquid pool 41, so as to avoid the overflow of flue gas. The upper part of the humidification treatment chamber 11 is provided with a second spray device 43, and the second spray device 43 is connected to the treatment liquid pool 41 through a delivery pipe through a second water pump 42 to recycle the treatment in the treatment liquid pool 41. The liquid sprays the flue gas entering from the flue gas inlet with a water bath to effectively remove sulfide and active nitrogen oxides in the flue gas. The spraying device 43 includes a spiral coil in the humidification treatment chamber 11, and a number of spray heads are arranged on the spiral coil, so that the smoke can be effectively contacted with the spray of the treatment liquid, and the dust in the smoke can be removed to the greatest extent. Sulfides and nitrogen oxides.
其中,所述处理液池41内盛装可循环利用的处理液,所述处理液可以是碱溶液,优选石灰水。在所述处理液池41内设置有水位监测传感器,当所述处理液池41内的处理液水位下降到一定程度时,发出报警或者添加处理液。Wherein, the treatment liquid pool 41 is filled with a recyclable treatment liquid, and the treatment liquid may be an alkali solution, preferably lime water. A water level monitoring sensor is provided in the treatment liquid pool 41, and when the water level of the treatment liquid in the treatment liquid pool 41 drops to a certain level, an alarm is issued or a treatment liquid is added.
所述过滤填料层13的厚度为25-40cm,其固定在所述处理塔的侧壁上。所述过滤填料层13内填充的是拉西环。所述拉西环尺寸为36mm~40mm。优选陶瓷拉西环,其陶瓷壁厚为4mm~8mm,价格低,且过滤效果明显。最优选的,所述过滤填料层13的厚度为33-36cm。The thickness of the filter packing layer 13 is 25-40 cm, which is fixed on the side wall of the treatment tower. The filter packing layer 13 is filled with Raschig rings. The size of the Raschig ring is 36mm-40mm. The ceramic Raschig ring is preferred, the ceramic wall thickness is 4mm-8mm, the price is low, and the filtering effect is obvious. Most preferably, the thickness of the filter packing layer 13 is 33-36 cm.
所述喷淋处理模块,在上述的基础上,所述加湿处理腔11为分级设置,所述加湿处理腔11内通过辅助过滤填料层15分割成最少两个子加湿处理腔(一级子加湿处理腔和二级子加湿处理腔)。所述一级子加湿处理腔和二级子加湿处理腔内分别设置所述喷淋装置43。烟气先通过一级子加湿处理腔喷淋处理后通过辅助过滤填料层15过滤后进入二级子加湿处理腔喷淋处理,然后通过过滤填料层13进行加湿后进入二次除尘腔12进行除尘处理。For the spray treatment module, on the basis of the above, the humidification treatment chamber 11 is arranged in stages, and the inside of the humidification treatment chamber 11 is divided into at least two sub-humidification treatment chambers (one sub-humidification treatment chamber) by auxiliary filter packing layer 15 chamber and secondary sub-humidification treatment chamber). The spraying devices 43 are respectively arranged in the first-level sub-humidification treatment chamber and the second-level sub-humidification treatment chamber. The flue gas is first sprayed through the primary humidification treatment chamber, then filtered through the auxiliary filter packing layer 15, and then enters the secondary humidification treatment chamber for spray treatment, then humidified through the filter packing layer 13, and then enters the secondary dust removal chamber 12 for dust removal deal with.
所述辅助过滤填料层15厚度为16-25cm,其固定在所述处理塔的侧壁上。所述过辅助过滤填料层15内填充的是鲍尔环。使用所述鲍尔环可以有效的节约20%-40%填料容积。最优选的,所述过滤填料层13的厚度为17-23cm。The auxiliary filter packing layer 15 has a thickness of 16-25 cm, and is fixed on the side wall of the treatment tower. Pall rings are filled in the auxiliary filter packing layer 15 . Using the Pall ring can effectively save 20%-40% of packing volume. Most preferably, the thickness of the filter packing layer 13 is 17-23 cm.
以上详细描述了本实用新型的较佳具体实施例,应当理解,本领域的普通技术无需创造性劳动就可以根据本实用新型的构思做出诸多修改和变化。因此,凡本技术领域中技术人员依本实用新型构思在现有技术基础上通过逻辑分析、推理或者根据有限的实验可以得到的技术方案,均应该在由本权利要求书所确定的保护范围之中。The preferred specific embodiments of the present utility model have been described in detail above, and it should be understood that those skilled in the art can make many modifications and changes according to the concept of the present utility model without creative work. Therefore, all technical solutions that can be obtained by those skilled in the art based on the concept of the utility model through logical analysis, reasoning or limited experiments on the basis of the prior art should be within the scope of protection defined by the claims .
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108619887A (en) * | 2018-05-17 | 2018-10-09 | 绍兴市鼎泰节能环保科技有限公司 | A kind of exhaust treatment system |
| CN109499258A (en) * | 2019-01-15 | 2019-03-22 | 李迎九 | A kind of vertical vehicle catalyst decomposition VOCs wind cabinet system |
| CN110732229A (en) * | 2019-11-14 | 2020-01-31 | 盐城市迎凯涂装设备有限公司 | post-coating-production engineering air purification system |
| CN111036019A (en) * | 2019-12-26 | 2020-04-21 | 崔建中 | Be applied to smokeless heat recovery unit of combustible waste recovery |
| CN112090202A (en) * | 2020-09-28 | 2020-12-18 | 滁州市汊河之星高新技术研发有限公司 | Harmful gas processing apparatus for environmental protection engineering |
| CN112973376A (en) * | 2021-03-04 | 2021-06-18 | 重庆新允创环保技术研究院有限公司 | Combined environment-friendly processing device for industrial waste gas treatment |
-
2017
- 2017-04-13 CN CN201720387240.0U patent/CN207024927U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108619887A (en) * | 2018-05-17 | 2018-10-09 | 绍兴市鼎泰节能环保科技有限公司 | A kind of exhaust treatment system |
| CN109499258A (en) * | 2019-01-15 | 2019-03-22 | 李迎九 | A kind of vertical vehicle catalyst decomposition VOCs wind cabinet system |
| CN110732229A (en) * | 2019-11-14 | 2020-01-31 | 盐城市迎凯涂装设备有限公司 | post-coating-production engineering air purification system |
| CN111036019A (en) * | 2019-12-26 | 2020-04-21 | 崔建中 | Be applied to smokeless heat recovery unit of combustible waste recovery |
| CN112090202A (en) * | 2020-09-28 | 2020-12-18 | 滁州市汊河之星高新技术研发有限公司 | Harmful gas processing apparatus for environmental protection engineering |
| CN112973376A (en) * | 2021-03-04 | 2021-06-18 | 重庆新允创环保技术研究院有限公司 | Combined environment-friendly processing device for industrial waste gas treatment |
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Granted publication date: 20180223 Termination date: 20200413 |