CN114768455A - Dust removal, defogging and composite adsorption material system testing method - Google Patents
Dust removal, defogging and composite adsorption material system testing method Download PDFInfo
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Abstract
Description
技术领域technical field
本发明是涉及到环保领域中对废气净化设备的除尘和除雾及复合吸附材料系统测试方法,尤其对含尘雾滴废气实施高效预处理装置与系统的去除粉尘和雾滴粒径大小、粉尘和雾滴浓度及测试与评估方法,其目的是提高对废气的净化技术及提升复合材料吸附的效果和使用寿命。The invention relates to a system testing method for dust removal and demisting of waste gas purification equipment and composite adsorption materials in the field of environmental protection, in particular to the removal of dust by a high-efficiency pretreatment device and system for dust-containing mist and droplet exhaust gas Droplet concentration and testing and evaluation methods, its purpose is to improve the purification technology of exhaust gas and improve the adsorption effect and service life of composite materials.
背景技术Background technique
在环保领域中废气净化装置和系统组合,对废气预处理装置起着承前启后的关键作用,为了弥补预处理装置和系统组合的缺陷和处理工艺上的短板,对除尘和除雾及复合吸附材料装置的各个工位及处理过程的临界流速和压损及接触时间等测试和评估方法有着至关重要的一面,用于改善与净化废气的构造和材料应用技术与方法,且能高效低成本适用于环保市场的需求。In the field of environmental protection, the combination of exhaust gas purification devices and systems plays a key role in linking the past and future of exhaust gas pretreatment devices. Test and evaluation methods such as critical flow rate, pressure loss and contact time of each station of the device and treatment process have a crucial aspect, and are used to improve and purify the structure and material application technology and method of exhaust gas, and can be applied with high efficiency and low cost. to meet the needs of the environmental protection market.
发明内容SUMMARY OF THE INVENTION
本发明是通过一系列技术特征解决上述的技术问题。The present invention solves the above-mentioned technical problems through a series of technical features.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:由污水槽、雾滴废气收集管、粉尘废气集气罩、粉尘废气收集管、集气管、负压式除尘器、排气管、带有喷淋一级除雾器、二级除雾器、风机、除尘除雾进气管、复合吸附材料装置、废气净化排气管、旁通排气管、调节风门、测试孔、粉尘粒径与浓度测试孔所组成。The test method for dust removal and fog removal and composite adsorption material system is characterized in that: a sewage tank, a mist drop exhaust gas collecting pipe, a dust exhaust gas collecting hood, a dust exhaust gas collecting pipe, a gas collecting pipe, a negative pressure type dust collector, a Air pipe, with spray primary demister, secondary demister, fan, dust removal and defogging intake pipe, composite adsorption material device, exhaust gas purification exhaust pipe, bypass exhaust pipe, regulating damper, test hole, It is composed of dust particle size and concentration test hole.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:在污水槽内设有污水管及在污水槽上部设有盖板,在盖板上部设置雾滴废气收集管用于收集污水槽流入污水处理过程中散发的、含雾滴(湿气)挥发性有机物废气;粉尘废气集气罩的锥形面吸气口设置在堆积工作台面上的粉尘、其距离收集粉尘的高度H为500~800mm之间,在锥形面的粉尘废气集气罩顶部设有粉尘废气收集管,设定粉尘废气集气罩的锥形面吸气口的气体流速应不小于0.3m/s;在雾滴废气收集管和粉尘废气收集管上分别设有调节风门、且与集气管相互连接,而集气管又分别与两组负压式除尘器进气管、风门a、雾滴废气旁通管、风门b、旁通排气管进行相互连接。The test method for dust removal and demisting and composite adsorption material system is characterized in that: a sewage pipe is arranged in the sewage tank and a cover plate is arranged on the upper part of the sewage tank, and a mist exhaust gas collecting pipe is arranged on the upper part of the cover plate for collecting sewage The tank flows into the waste gas containing mist (moisture) volatile organic compounds emitted during the sewage treatment process; the conical surface suction port of the dust exhaust gas collecting hood is set on the dust accumulation worktable, and the height H from the collected dust is Between 500mm and 800mm, a dust and exhaust gas collection pipe is arranged on the top of the dust and exhaust gas collecting hood on the conical surface, and the gas flow rate at the suction port of the conical surface of the dust and exhaust gas collecting hood shall not be less than 0.3m/s; The mist exhaust gas collection pipe and the dust exhaust gas collection pipe are respectively provided with regulating dampers, which are connected with the gas collection pipes, and the gas collection pipes are respectively connected with two sets of negative pressure dust collector intake pipes, dampers a, mist drop exhaust gas bypass pipes, The damper b and the bypass exhaust pipe are connected to each other.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:两组负压式除尘器进气管上分别设有调节风门和用于除尘器筒体内粉尘的、冲洗用喷嘴与喷淋水管与喷淋调节水阀相连接;两组负压式除尘器除尘管出口处设有调节风门与排气管相连接,其排气管又与雾滴废气旁通管、风门c、带有喷淋一级除雾器、二级除雾器的进口端和出口端、风机的进口端相连接;风机的出口端设有除尘除雾进气管与旁通排气管a及风门d和风门e之间进行相互连接;除尘除雾进气管设有调节风门又与复合吸附材料装置的进口端相连接。The test method for dust removal and fog removal and composite adsorption material system is characterized in that: two sets of negative pressure dust collector air intake pipes are respectively provided with adjustment dampers, and flushing nozzles and sprays for dust in the dust collector cylinder. The water pipe is connected with the spray regulating water valve; the outlet of the two sets of negative pressure dust collectors is provided with a regulating air valve and the exhaust pipe is connected, and the exhaust pipe is connected with the droplet waste gas bypass pipe, the air valve c, and the exhaust pipe. The inlet and outlet ends of the spray primary demister and the secondary demister are connected to the inlet end of the fan; the outlet end of the fan is provided with a dust removal and demisting intake pipe, a bypass exhaust pipe a, a damper d and a damper e are connected with each other; the dust-removing and mist-removing air intake pipe is provided with a regulating damper and is connected with the inlet end of the composite adsorption material device.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:在复合吸附材料装置内设有经过改良与改性而制成的活性炭吸附材料,装填有酸性吸附材料盒、中性吸附材料盒、碱性吸附材料盒为三层、称之为复合吸附材料,还设有用于吊装装填有复合吸附材料盒进出口的手动葫芦;在酸性吸附材料盒的下部进口端设有除尘除雾进气管和调节风门,在碱性吸附材料盒上部出口端设有废气净化排气管和调节风门,除尘除雾进气管与废气净化排气管的调节风门相互连接;通过风机出口端连接除尘除雾进气管及旁通排气管a,旁通排气管a又和旁通排气管与废气净化排气管进行相互连接组和成一套除尘和除雾及复合吸附材料系统。The method for testing dust removal and fog removal and composite adsorption material system is characterized in that: the composite adsorption material device is provided with an activated carbon adsorption material made of improvement and modification, filled with an acid adsorption material box, a neutral adsorption material The material box and the alkaline adsorption material box are three-layered, which are called composite adsorption materials. There is also a manual hoist for hoisting and filling the inlet and outlet of the composite adsorption material box; the lower inlet end of the acid adsorption material box is equipped with dust removal and fog removal. The air intake pipe and the adjusting air valve are provided with the exhaust gas purification exhaust pipe and the adjusting air valve at the upper outlet end of the alkaline adsorption material box. The mist intake pipe and the bypass exhaust pipe a, the bypass exhaust pipe a and the bypass exhaust pipe and the exhaust gas purification exhaust pipe are connected to each other to form a set of dust removal and fog removal and composite adsorption material system.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:在两组负压式除尘器的下部均设有三相分离器是用于含尘雾滴废气中的气固液分离;三相分离器内部设有固液分离滤网,在三相分离器的下部还设有排水阀和排尘管分别用于液体与固体物的单独排放;两组负压式除尘器与三相分离器作为一个整体设备设置在集尘水槽的上部左侧部位;带有喷淋一级除雾器进口处设有用于除雾器内、除雾用喷嘴与喷淋水管连接喷淋调节水阀;带有喷淋一级除雾器内设有一级除雾过滤模块和排水用的排水阀门与一级除雾器排水管及支架;二级除雾器内设有二级除雾过滤模块和排水用的排水阀门和二级除雾器排水管及二级除雾器支架;带有喷淋一级除雾器设置在集尘水槽上部的右侧部位,一级除雾器排水管设有大于2倍以上管径的凸型部位用于水封,一级除雾器排水管的排水口一端与集尘水槽顶部的入水口相互连接,而二级除雾器则依靠二级除雾器支架单独设置在地面上用紧固件予以固定,在二级除雾器排水管设有大于2倍以上管径的凸型部位用于水封,二级除雾器排水管的排水出口处设有排水桶。The test method for dust removal and demisting and composite adsorption material system is characterized in that: a three-phase separator is arranged at the lower part of the two sets of negative pressure type dust collectors for gas-solid-liquid separation in the waste gas containing dust mist droplets; three There is a solid-liquid separation filter screen inside the phase separator, and a drain valve and a dust discharge pipe are also arranged at the lower part of the three-phase separator for separate discharge of liquid and solid matter; two sets of negative pressure dust collectors are separated from the three-phase separator. As a whole device, the demister is installed on the upper left part of the dust collecting tank; the inlet of the first-level demister with spray is provided with a spray regulating water valve for connecting the mist eliminator, the nozzle for demisting and the spray water pipe; The primary demister with spray is equipped with a primary demister filter module and drain valve for drainage, as well as the primary demister drain pipe and bracket; the secondary demister is provided with a secondary demister filter module and drainage The drain valve and the secondary demister drain pipe and the secondary demister bracket are used; the primary demister with spray is arranged on the right side of the upper part of the dust collecting tank, and the primary demister drain pipe is provided with a The convex part with more than 2 times the pipe diameter is used for water sealing. One end of the drain port of the primary demister drain pipe is connected to the water inlet at the top of the dust collecting tank, and the secondary demister relies on the secondary demister bracket. It is set separately on the ground and fixed with fasteners. The drain pipe of the secondary mist eliminator is provided with a convex part with a diameter of more than 2 times for water sealing. Drain bucket.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:在雾滴废气收集管、集气管、排气管、除尘除雾进气管、废气净化排气管上设有测试孔,在粉尘废气收集管、负压式除尘器进气管、负压式除尘器除尘管上设有粉尘粒径与浓度测试孔;测试孔的口径为DN80,通过法兰外接一个带有法兰的DN40变径接头,其长度被测试的管道中心至变径接头的法兰面之间距离设置最小不低于360mm;粉尘粒径与浓度测试孔的口径为DN80,其长度被测试的管道中心至测试孔的法兰面之间距离设置最小不低于180mm;在雾滴废气收集管、粉尘废气收集管、集气管、除尘除雾进气管、废气净化排气管上测试孔所设置的距离、与位于带有喷淋一级除雾器及二级除雾器的进气端和排气端法兰面与测试孔中心的M和N距离、分别设置为6倍及6倍以上、3倍及3倍以上管径直径尺寸距离后组合成一套用于除尘和除雾及废气净化系统能力的测试方法。The test method for dust removal and fog removal and composite adsorption material system is characterized in that: test holes are provided on the mist drop exhaust gas collection pipe, the gas collector pipe, the exhaust pipe, the dust removal and mist removal air intake pipe, and the exhaust gas purification exhaust pipe, There are dust particle size and concentration test holes on the dust exhaust gas collection pipe, the intake pipe of the negative pressure type dust collector and the dust removal pipe of the negative pressure type dust collector; the diameter of the test hole is DN80, and a DN40 with flange is connected through the flange For reducing joints, the distance from the center of the pipeline to be tested to the flange surface of the reducing joint shall be set at a minimum of 360mm; the diameter of the dust particle size and concentration test hole is DN80, and its length is from the center of the pipeline to be tested to the test hole. The minimum distance between the flange surfaces of the holes is set to be no less than 180mm; the distance set by the test holes on the droplet exhaust gas collection pipe, the dust exhaust gas collection pipe, the gas collection pipe, the dust removal and defogging intake pipe, and the exhaust gas purification exhaust pipe shall be the same as the distance between the test holes. The distances M and N between the flange faces of the inlet and exhaust ends with the spray primary demister and secondary demister and the center of the test hole are set to 6 times and above, 3 times and A set of test methods for dust removal and demisting and exhaust gas purification system capabilities are combined after more than 3 times the diameter of the pipe diameter.
所述的除尘和除雾及复合吸附材料系统测试方法,其特征在于:集尘水槽作为除尘与除雾系统测试过程中排水的辅助设备,在集尘水槽内中部设置中间隔板分为两个水槽,在隔板的中心出上低于水位50mm处设有V型开口;在集尘水槽底部的不同位置设有水槽排水管a和水槽排水管b及排水阀门,在集尘水槽内水位上面设有水槽进水管及进水阀门;把水槽排水管a和水槽排水管b用管道进行相互连接、可外接排水泵和排水管道组合成排水系统;当负压式除尘器和三相分离器及除雾器,把含尘雾滴的挥发性有机物实施气固液分离后的污水流入到集尘水槽内,通过排水系统再把污水经过达标处理后向外排放。The test method for dust removal and fog removal and composite adsorption material system is characterized in that: the dust collecting water tank is used as auxiliary equipment for drainage during the test process of the dust collecting and fog removal system, and a middle partition plate is arranged in the middle of the dust collecting water tank and is divided into two parts. For the water tank, there is a V-shaped opening at the center of the partition plate 50mm below the water level; there are water tank drain pipes a, water tank drain pipes b and drain valves at different positions at the bottom of the dust collection tank, above the water level in the dust collection tank Equipped with a water tank inlet pipe and water inlet valve; the water tank drain pipe a and the water tank drain pipe b are connected to each other with pipes, and an external drain pump and drain pipe can be combined to form a drainage system; when the negative pressure dust collector and the three-phase separator and The mist eliminator, the sewage after the gas-solid-liquid separation of volatile organic compounds containing dust mist droplets is carried out into the dust collection tank, and the sewage is discharged through the drainage system after reaching the standard treatment.
本发明的测试方法简单合理,其测试流程方法1是:所述的除尘和除雾及复合吸附材料系统测试方法,用雾滴废气收集管对含雾滴(湿气)挥发性有机物的收集,用粉尘废气集气罩和粉尘废气收集管对粉尘的收集,通过集气管连接雾滴废气收集管与粉尘废气收集管把收集到的含尘雾滴废气、流经负压式除尘器与带有喷淋一级除雾器及二级除雾器预处理,风机把除尘除雾的挥发性有机物经由除尘除雾进气管送入复合吸附材料装置内实施复合吸附材料化学平衡净化处理后、流经废气净化排气管向外排放;在雾滴废气收集管、粉尘废气收集管、集气管、排气管、除尘除雾进气管、废气净化排气管、旁通排气管上设置的测试孔,用粉尘与雾滴测试仪分别测试含尘雾滴废气粒径和浓度及除尘除雾废气与复合吸附材料的各个装置净化能力。The test method of the present invention is simple and reasonable, and the test process method 1 is: the described dust removal and demisting and composite adsorption material system test method, the collection of volatile organic compounds containing mist droplets (moisture) with a mist exhaust gas collection pipe, Use the dust exhaust gas collecting hood and the dust exhaust gas collection pipe to collect the dust, connect the mist drop exhaust gas collection pipe and the dust exhaust gas collection pipe through the gas collection pipe, and pass the collected dust-containing mist droplet exhaust gas through the negative pressure dust collector and with the spray. The first-level mist eliminator and the second-level mist eliminator are used for pretreatment, and the fan sends the volatile organic compounds from dust removal and mist removal into the composite adsorption material device through the dust removal and demisting air intake pipe for chemical equilibrium purification treatment of the composite adsorption material, and flows through the exhaust gas. The purification exhaust pipe is discharged to the outside; the test holes set on the mist exhaust gas collection pipe, the dust exhaust gas collection pipe, the gas collecting pipe, the exhaust pipe, the dust removal and defogging intake pipe, the exhaust gas purification exhaust pipe and the bypass exhaust pipe, Use a dust and droplet tester to test the particle size and concentration of dust-containing droplet exhaust gas and the purification capacity of each device for dust-removing and mist-removing exhaust gas and composite adsorption materials.
本发明的测试方法简单合理,其测试流程方法2是:所述的除尘和除雾及复合吸附材料系统测试方法,采用单独测试含雾滴废气粒径和浓度的方法是:首先关闭粉尘废气收集管和负压式除尘器进气管及负压式除尘器除尘管上设置的调节风门、打开集气管上的风门a和雾滴废气旁通管上设置的风门c、关闭集气管上的风门b,当雾滴废气收集管对污水槽处理过程中散发的含雾滴(湿气)挥发性有机物收集后经由集气管、雾滴废气收集管流入到排气管经由带有喷淋一级除雾器及二级除雾器,再通过风机和除尘除雾进气管的抽引与压送到复合吸附材料装置进行处理和用测试仪器、在测试孔对流入的含雾滴(湿气)挥发性有机物和系统净化后的出口测试得到去除雾滴粒径和浓度及废气净化的效率。The test method of the present invention is simple and reasonable, and the test process method 2 is: the method for testing the dust removal and demisting and composite adsorption material system, and the method for testing the particle size and concentration of the exhaust gas containing mist droplets separately is: firstly, close the dust exhaust gas collection Adjust the damper set on the inlet pipe of the negative pressure type dust collector and the dust removal pipe of the negative pressure type dust collector, open the damper a on the collecting pipe and the damper c set on the droplet waste gas bypass pipe, and close the damper b on the gas collecting pipe , when the droplet waste gas collection pipe collects the volatile organic compounds containing droplets (moisture) emitted during the treatment of the sewage tank, it flows into the exhaust pipe through the gas collection pipe and the droplet waste gas collection pipe and passes through the first-level demisting with spraying. It is then sent to the composite adsorption material device through the suction and pressure of the fan and the dust removal and demisting air intake pipe for processing and the test instrument is used to measure the volatility of the inflowing droplets (moisture) in the test hole. Outlet testing of organics and system purification yields the removal of droplet size and concentration and the efficiency of exhaust gas purification.
本发明的测试方法简单合理,其测试流程方法3是:所述的除尘和除雾及复合吸附材料系统测试方法,采用单独测试粉尘粒径和浓度的方法是,首先关闭雾滴废气收集管上设置的调节风门和集气管上的风门a及风门b与雾滴废气旁通管上的风门c,还有关闭雾滴废气旁通管a上设置的风门e、除尘除雾进气管和废气净化排气管上设置的调节风门;打开粉尘废气集气罩相连接粉尘废气收集管上设置的调节风门、负压式除尘器进气管和负压式除尘器除尘管上的调节风门、雾滴废气旁通管a上设置的风门d;当粉尘废气集气罩相连接粉尘废气收集管对粉尘收集后,经由集气管分别流入到两组负压式除尘器内除尘处理、再通过排气管经由带有喷淋一级除雾器及二级除雾器、风机的抽引与压送到除尘除雾进气管、雾滴废气旁通管a与旁通排气管排出过程中,用测试仪器在粉尘粒径与浓度测试孔及测试孔对流入的粉尘经过处理净化后出口的测试得到去除粉尘粒径和浓度及废气净化的效率。The test method of the present invention is simple and reasonable, and the
附图说明Description of drawings
图1为本发明装置所实施的立面视图;Fig. 1 is the elevation view of the device of the present invention implemented;
图2为图1中的平面视图;Fig. 2 is a plan view in Fig. 1;
图中标记说明Description of the marks in the figure
图1中:In Figure 1:
1-除尘和除雾及复合吸附材料系统测试方法,2-污水槽,3-雾滴废气收集管,4-调节风门,5-测试孔,6-粉尘,7-粉尘废气集气罩,8-粉尘废气收集管,9-粉尘粒径与浓度测试孔,10-集气管,11-负压式除尘器,12-负压式除尘器进气管,12a-冲洗用喷嘴与喷淋水管,13-负压式除尘器除尘管,14-排气管,15-带有喷淋一级除雾器,15a-一级除雾器除雾过滤模块,15b-除雾用喷嘴与喷淋水管,15c-一级除雾器排水管,16-二级除雾器,16a-二级除雾器除雾过滤模块,16b-二级除雾器排水管,16c-二级除雾器支架,16d-排水桶,17-风机,18-除尘除雾进气管,19-复合吸附材料装置,19a-酸性吸附材料盒,19b-中性吸附材料盒,19c-碱性吸附材料盒,19d-复合吸附材料吊装葫芦,20-废气净化排气管,21-风门a,22-雾滴废气旁通管,23-风门b,24-旁通排气管,25-三相分离器,25a-固液分离滤网,25b-排尘管,25c-分离器排水管与排水阀门,26-集尘水槽,26a-水槽排水管a,26b-水槽排水管b,26c-水槽进水管,27-风门c,31-旁通排气管a,32-风门d,33-风门e。1- Test method for dust removal and defogging and composite adsorption material system, 2- sewage tank, 3- mist drop exhaust gas collection pipe, 4- regulating damper, 5- test hole, 6- dust, 7- dust exhaust gas collecting hood, 8 -Dust exhaust gas collection pipe, 9- Dust particle size and concentration test hole, 10-Gas collection pipe, 11-Negative pressure type dust collector, 12-Negative pressure type dust collector intake pipe, 12a-Nozzle for flushing and spray water pipe, 13- -Dedusting pipe of negative pressure dust collector, 14-exhaust pipe, 15-with spray first-level mist eliminator, 15a-first-level mist eliminator demisting filter module, 15b-nozzle and spray water pipe for demisting, 15c- Primary demister drain pipe, 16- Secondary demister, 16a- Secondary demister demister filter module, 16b- Secondary demister drain, 16c- Secondary demister bracket, 16d -Drain bucket, 17-Fan, 18-Dust and defogging intake pipe, 19-Composite adsorption material device, 19a-Acid adsorption material box, 19b-Neutral adsorption material box, 19c-Alkaline adsorption material box, 19d-Composite adsorption Materials Lifting hoist, 20-exhaust gas purification exhaust pipe, 21-air valve a, 22-mist drop exhaust gas bypass pipe, 23-air valve b, 24-bypass exhaust pipe, 25-three-phase separator, 25a-solid-liquid Separation screen, 25b-dust pipe, 25c-separator drain and drain valve, 26-dust collection tank, 26a-sink drain a, 26b-sink drain b, 26c-sink inlet pipe, 27- damper c , 31 - bypass exhaust pipe a, 32 - damper d, 33 - damper e.
图2中:In Figure 2:
1-除尘和除雾及复合吸附材料系统测试方法,2-污水槽,3-雾滴废气收集管,4-调节风门,5-测试孔,7-粉尘废气集气罩,8-粉尘废气收集管,9-粒径与粉尘浓度测试孔,10-集气管,11-负压式除尘器,12-负压式除尘器进气管,12a-冲洗用喷嘴与喷淋水管,13-负压式除尘器排气管,14-排气管,15-带有喷淋一级除雾器,15a-一级除雾过滤模块,15b-除雾用喷嘴与喷淋水管,15c-一级除雾器排水管,16-二级除雾器,16a-二级除雾过滤模块,16b-二级除雾器排水管,16c-二级除雾器支架,17-风机,18-除尘除雾进气管,19-复合吸附材料装置,19a-酸性复合吸附材料,19b-中性复合吸附材料,19c-碱性复合吸附材料,19d-手动葫芦,20-废气净化排气管,21-风门a,22-旁通雾滴废气管,23-风门b,24-旁通排气管,25-三相分离器,25a-固液分离滤网,26-集尘水槽,26a-水槽排水管,26b-水槽排水管b,26c-水槽进水管,27-风门c,31-旁通排气管a,32-风门d,33-风门e。1- Test method for dust removal and demisting and composite adsorption material system, 2- Sewage tank, 3- Mist exhaust gas collection pipe, 4- Adjusting damper, 5- Test hole, 7- Dust exhaust gas collecting hood, 8- Dust exhaust gas collection Pipe, 9-Particle size and dust concentration test hole, 10-Gas collection pipe, 11-Negative pressure type dust collector, 12-Negative pressure type dust collector inlet pipe, 12a-Nozzle and spray water pipe for flushing, 13-Negative pressure type Dust collector exhaust pipe, 14-exhaust pipe, 15-first-stage mist eliminator with spray, 15a-first-stage demisting filter module, 15b-nozzle and spray water pipe for demisting, 15c-first-stage demisting 16-secondary demister, 16a-secondary demister filter module, 16b-secondary demister drain, 16c-secondary demister bracket, 17-fan, 18-dust and defogger inlet Trachea, 19-composite adsorption material device, 19a-acid composite adsorption material, 19b-neutral composite adsorption material, 19c-alkaline composite adsorption material, 19d-manual hoist, 20-exhaust gas purification exhaust pipe, 21-air valve a, 22- Bypass mist exhaust pipe, 23- Damper b, 24- Bypass exhaust pipe, 25- Three-phase separator, 25a- Solid-liquid separation filter, 26- Dust collection tank, 26a- Water tank drain pipe, 26b -Sink drain pipe b, 26c-Sink inlet pipe, 27- Damper c, 31-Bypass exhaust pipe a, 32- Damper d, 33- Damper e.
具体实施方式Detailed ways
下面结合实施例和附图对本发明的技术特征作进一步说明。The technical features of the present invention will be further described below with reference to the embodiments and the accompanying drawings.
依据图1、图2所示,所述的除尘和除雾及复合吸附材料系统测试方法1,由污水槽2,雾滴废气收集管3,粉尘废气集气罩7,粉尘废气收集管8,集气管10,负压式除尘器11,排气管14,带有喷淋一级除雾器15,二级除雾器16,风机17,除尘除雾进气管18,旁通排气管24,复合吸附材料装置19,废气净化排气管20,调节风门4,测试孔5、粒径与粉尘浓度测试孔9所组成;在污水槽2内设有污水管及在污水槽2的上部设有盖板,在盖板上部设置的雾滴废气收集管3是用于收集污水槽2流入污水处理过程中散发的、含雾滴(湿气)挥发性有机物废气;粉尘废气集气罩7的锥形面吸气口设置在堆积工作台面上的粉尘6、其距离收集粉尘6的高度H为500~800mm之间,在锥形面的粉尘废气集气罩7上顶部设有粉尘废气收集管8,设定粉尘废气集气罩7的锥形面吸气口的气体流速应不小于0.3m/s;雾滴废气收集管3和粉尘废气收集管8分别设有调节风门4且与集气管10相互连接,而集气管10又分别与两组负压式除尘器进气管11、风门a21、雾滴废气旁通管22、风门b23、旁通排气管24进行相互连接;两组负压式除尘器进气管12上分别设有调节风门4和用于负压式除尘器11筒体内粉尘的、冲洗用喷嘴与喷淋水管12a与喷淋调节水阀连接;两组负压式除尘器除尘管13出口处设有调节风门4与排气管14相连接,其排气管14又与雾滴废气旁通管22、风门c27、带有喷淋一级除雾器15、二级除雾器16的进口端和出口端、风机17的进口端相连接;风机17的出口端设有除尘除雾进气管18与旁通排气管a31及风门d32和风门e33之间进行相互连接;除尘除雾进气管18设有调节风门4又与复合吸附材料装置19的进口端相连接;在复合吸附材料装置19内设有经过改良与改性而制成的活性炭吸附材料,装填有酸性吸附材料盒19a、中性吸附材料盒19b、碱性吸附材料盒19c为三层、称之为复合吸附材料,还设有用于吊装装填有复合吸附材料盒进出口的手动葫芦19d;在酸性吸附材料盒19a的下部进口端设有除尘除雾进气管18和调节风门4,在碱性吸附材料盒19c上部出口端设有废气净化排气管20和调节风门4,除尘除雾进气管18与废气净化排气管20的调节风门4相互连接;通过风机17出口端连接除尘除雾进气管18及旁通排气管a31,旁通排气管a31又和旁通排气管24与废气净化排气管24进行相互连接组和成一套除尘和除雾及复合吸附材料系统。According to Fig. 1 and Fig. 2, the test method 1 for dust removal and demisting and composite adsorption material system consists of a sewage tank 2, a mist drop exhaust
依据图1、图2所示,所述的除尘和除雾及复合吸附材料系统测试方法1,在两组负压式除尘器11的下部均设有三相分离器25是用于含尘雾滴废气中的气固液分离;三相分离器25内部设有固液分离滤网25a,在三相分离器25的下部还设有排水阀25c和排尘管25b分别用于液体与固体物的单独排放;两组负压式除尘器11与三相分离器25作为一个整体设备设置在集尘水槽26的上部左侧部位;带有喷淋一级除雾器15进口处设有用于除雾器内、除雾用喷嘴与喷淋水管15b连接喷淋调节水阀;带有喷淋一级除雾器15内设有一级除雾过滤模块15a和排水用的排水阀门与一级除雾器排水管15c及支架;二级除雾器内16设有二级除雾过滤模块16a和排水用的排水阀门和二级除雾器排水管16b及二级除雾器支架16c;带有喷淋一级除雾器15设置在集尘水槽26上部的右侧部位,一级除雾器排水管16b设有大于2倍以上管径的凸型部位用于水封,一级除雾器排水管15c的排水口一端与集尘水槽26顶部的入水口相互连接,而二级除雾器16则依靠二级除雾器支架16c单独设置在地面上用紧固件予以固定,在二级除雾器排水管16b设有大于2倍以上管径的凸型部位用于水封,二级除雾器排水管16b的排水出口处设有排水桶16d;在雾滴废气收集管3、集气管10、排气管14、除尘除雾进气管18、废气净化排气管20上设有测试孔5,在粉尘废气收集管8、负压式除尘器进气管12、负压式除尘器除尘管13上设有粉尘粒径与浓度测试孔9;测试孔5的口径为DN80,通过法兰外接一个带有法兰的DN40变径接头,其长度被测试的管道中心至变径接头的法兰面之间距离设置最小不低于360mm;粉尘粒径与浓度测试孔9的口径为DN80,其长度被测试的管道中心至测试孔的法兰面之间距离设置最小不低于180mm;在雾滴废气收集管3、粉尘废气收集管8、集气管10、除尘除雾进气管18、废气净化排气管20上测试孔5所设置的距离、与位于带有喷淋一级除雾器15及二级除雾器16的进气端和排气端法兰面与测试孔5中心的M和N距离、分别设置为6倍及6倍以上、3倍及3倍以上管径直径尺寸距离后组合成一套用于除尘和除雾及废气净化系统能力的测试方法。According to Figures 1 and 2, the test method 1 for the dust removal and demisting and composite adsorption material system, a three-
本发明的测试方法简单合理,其测试流程方法1是:所述的除尘和除雾及复合吸附材料系统测试方法1,用雾滴废气收集管3对含雾滴(湿气)挥发性有机物的收集,用粉尘废气集气罩7和粉尘废气收集管8对粉尘6的收集,通过集气管10连接雾滴废气收集管3与粉尘废气收集管8把收集到的含尘雾滴废气、流经负压式除尘器11与带有喷淋一级除雾器15及二级除雾器16预处理,风机17把除尘除雾的挥发性有机物经由除尘除雾进气管18送入复合吸附材料装置19内实施复合吸附材料化学平衡净化处理后、流经废气净化排气管20向外排放;在雾滴废气收集管3、粉尘废气收集管8、集气管10、排气管14、除尘除雾进气管18、废气净化排气管20、旁通排气管24上设置的测试孔5,用粉尘6与雾滴测试仪分别测试含尘雾滴废气粒径和浓度及除尘除雾废气与复合吸附材料的各个装置净化能力。The test method of the present invention is simple and reasonable, and the test process method 1 is: the test method 1 of the dust removal and demisting and composite adsorption material system, using the mist drop exhaust
本发明的测试方法简单合理,其测试流程方法2是:所述的除尘和除雾及复合吸附材料系统测试方法1,采用单独测试含雾滴废气粒径和浓度的方法是:首先关闭粉尘废气收集管8和负压式除尘器进气管12及负压式除尘器除尘管13上设置的调节风门4、打开集气管10上的风门a21和雾滴废气旁通管22上设置的风门c27、关闭集气管10上的风门b23,当雾滴废气收集管3对污水槽2处理过程中散发的含雾滴(湿气)挥发性有机物收集后、经由集气管10、雾滴废气收集管3流入到排气管14经由带有喷淋一级除雾器15及二级除雾器16,再通过风机17和除尘除雾进气管18的抽引与压送到复合吸附材料装置19进行处理和用测试仪器、在测试孔5对流入的含雾滴(湿气)挥发性有机物和系统净化后的出口测试得到去除雾滴粒径和浓度及废气净化的效率。The test method of the present invention is simple and reasonable, and its test flow method 2 is: the described dust removal and demisting and composite adsorption material system test method 1, the method of using a separate test for the particle size and concentration of the exhaust gas containing mist is: firstly close the dust exhaust gas The collecting
本发明的测试方法简单合理,其测试流程方法3是:所述的除尘和除雾及复合吸附材料系统测试方法1,采用单独测试粉尘6粒径和浓度的方法是,首先关闭雾滴废气收集管3上设置的调节风门4和集气管10上的风门a21及风门b23与雾滴废气旁通管22上的风门c27,还有关闭雾滴废气旁通管a31上设置的风门e33、除尘除雾进气管18和废气净化排气管20上设置的调节风门4;打开粉尘废气集气罩7相连接粉尘废气收集管8上设置的调节风门4、负压式除尘器进气管12和负压式除尘器除尘管13上的调节风门4、雾滴废气旁通管a31上设置的风门d32;当粉尘废气集气罩7相连接粉尘废气收集管8对粉尘6收集后,经由集气管10分别流入到两组负压式除尘器11内进行除尘处理、再通过排气管14经由带有喷淋一级除雾器15及二级除雾器16、风机17的抽引与压送到除尘除雾进气管18、雾滴废气旁通管a31与旁通排气管24排出过程中,用测试仪器在粉尘粒径与浓度测试孔9及测试孔5对流入的粉尘6经过处理净化后出口的测试得到去除粉尘6粒径和浓度及废气净化的效率。The test method of the present invention is simple and reasonable, and the test flow method 3 is: the described dust removal and demisting and composite adsorption material system test method 1, adopting the method of individually testing the particle size and concentration of the dust 6 is, firstly, close the mist drop exhaust gas collection The regulating damper 4 set on the pipe 3, the damper a21 and the damper b23 on the air collecting pipe 10, and the damper c27 on the droplet waste gas bypass pipe 22, and closing the damper e33 set on the droplet waste gas bypass pipe a31, dust removal The adjustment damper 4 set on the mist intake pipe 18 and the exhaust gas purification exhaust pipe 20; open the dust exhaust gas collecting hood 7 to connect the adjustment damper 4 set on the dust exhaust gas collecting pipe 8, the air intake pipe 12 of the negative pressure type dust collector and the negative pressure The regulating damper 4 on the dust removal pipe 13 of the dust collector, and the damper d32 set on the droplet exhaust gas bypass pipe a31; It flows into the two sets of negative pressure dust collectors 11 for dust removal treatment, and then passes through the exhaust pipe 14 and is sent to dust removal through the extraction and pressure of the first-level mist eliminator 15 and the second-level mist eliminator 16 and the fan 17. During the discharge process of the defogging intake pipe 18, the mist droplet exhaust gas bypass pipe a31 and the
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Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101293108A (en) * | 2007-04-26 | 2008-10-29 | 陈妙生 | Deodorizing method of hydrogen sulphide removing material and absorbent charcoal adsorption, and processing equipment |
CN214319703U (en) * | 2020-11-02 | 2021-10-01 | 唐锦婷 | Production technology processing system |
CN113521943A (en) * | 2021-06-29 | 2021-10-22 | 宁波明讯实业有限公司 | Small-air-volume automobile spray paint and automobile plastic modified waste gas treatment process |
CN217613837U (en) * | 2022-05-20 | 2022-10-21 | 山东建筑大学 | Dust and mist removal and composite adsorbent material systems |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101293108A (en) * | 2007-04-26 | 2008-10-29 | 陈妙生 | Deodorizing method of hydrogen sulphide removing material and absorbent charcoal adsorption, and processing equipment |
CN214319703U (en) * | 2020-11-02 | 2021-10-01 | 唐锦婷 | Production technology processing system |
CN113521943A (en) * | 2021-06-29 | 2021-10-22 | 宁波明讯实业有限公司 | Small-air-volume automobile spray paint and automobile plastic modified waste gas treatment process |
CN217613837U (en) * | 2022-05-20 | 2022-10-21 | 山东建筑大学 | Dust and mist removal and composite adsorbent material systems |
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