CN208130662U - Paint spray booth's organic waste gas treatment system - Google Patents

Paint spray booth's organic waste gas treatment system Download PDF

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CN208130662U
CN208130662U CN201721911330.1U CN201721911330U CN208130662U CN 208130662 U CN208130662 U CN 208130662U CN 201721911330 U CN201721911330 U CN 201721911330U CN 208130662 U CN208130662 U CN 208130662U
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desorption
adsorption
valve
waste gas
absorption
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蒋伟
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Jiangsu Yongyi Environmental Protection Technology Co Ltd
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Abstract

本实用新型公开了一种喷漆室有机废气处理系统,包括干式过滤器、吸附脱附箱、催化燃烧装置、吸附风机、脱附风机和补气风机,吸附脱附箱设有三个,催化燃烧装置内设有预热室、催化床、换热器和第一热电偶,预热室内具有加热器;还包括PLC控制系统,PLC控制系统包括PLC控制器、安装于吸附脱附箱的第一热电偶以及第一超温报警器、安装于所述催化燃烧装置的第二超温报警器和设于所述干式过滤器的压差计,所述PLC控制器安装于控制柜。本实用新型解决了喷漆废气易堵塞、废气不能稳定达标的问题,且系统的自动化和智能化程度高,对废气的处理效果佳,净化效率>98%,满足并高于国家排放标准;且能够在线对废气催化燃烧处理,实现废气的零排放。

The utility model discloses a treatment system for organic waste gas in a painting room, which comprises a dry filter, an adsorption and desorption box, a catalytic combustion device, an adsorption fan, a desorption fan and an air supply fan, three adsorption and desorption boxes are provided, and the catalytic combustion The device is equipped with a preheating chamber, a catalytic bed, a heat exchanger and a first thermocouple. There is a heater in the preheating chamber; it also includes a PLC control system, which includes a PLC controller and a first thermocouple installed in the adsorption and desorption box. A thermocouple, a first over-temperature alarm, a second over-temperature alarm installed in the catalytic combustion device, and a differential pressure gauge installed in the dry filter, and the PLC controller is installed in a control cabinet. The utility model solves the problems that the waste gas from spray painting is easy to block and the waste gas cannot reach the standard stably, and the system has a high degree of automation and intelligence, has a good treatment effect on the waste gas, and has a purification efficiency of >98%, which meets and is higher than the national discharge standard; and can On-line catalytic combustion treatment of exhaust gas to achieve zero emission of exhaust gas.

Description

喷漆室有机废气处理系统Organic waste gas treatment system in spray booth

技术领域technical field

本实用新型涉及废气处理技术领域,特别是涉及一种喷漆室的废气处理系统。The utility model relates to the technical field of exhaust gas treatment, in particular to an exhaust gas treatment system for a spray booth.

背景技术Background technique

喷漆废气的主要成分是喷漆粉尘及挥发的苯、甲苯、二甲苯等,随意排放对周围环境有一定影响,因此,需要进行一定的处理后排放。The main components of spray paint exhaust gas are paint spray dust and volatilized benzene, toluene, xylene, etc. Random discharge will have a certain impact on the surrounding environment. Therefore, it needs to be discharged after certain treatment.

传统处理工艺流程主要为:喷漆废气→水喷淋塔→干湿分离→初效过滤器→活性炭吸附→排放。The traditional treatment process mainly includes: paint exhaust gas→water spray tower→dry-wet separation→primary effect filter→activated carbon adsorption→discharge.

由于漆粉具有粘性,采用活性炭吸附处理有机废气,活性炭吸附饱和以后采用催化燃烧对其进行脱附,喷漆室排出的尾气中含定量漆雾,属于粘性物质,所以在废气进入活性炭吸附装置前必须要进行预处理,否则,废气进入活性炭吸附装置会造成不必要的麻烦,甚至使活性炭失效,因为废气中的粘性颗粒容易使活性炭“堵死”。Due to the viscosity of paint powder, activated carbon adsorption is used to treat organic waste gas. After the activated carbon is saturated, catalytic combustion is used to desorb it. The exhaust gas discharged from the spray booth contains a certain amount of paint mist, which is a viscous substance. Therefore, before the exhaust gas enters the activated carbon adsorption device, it must be Pretreatment must be carried out, otherwise, the exhaust gas entering the activated carbon adsorption device will cause unnecessary trouble, and even make the activated carbon invalid, because the sticky particles in the exhaust gas will easily "block" the activated carbon.

比如中国专利《喷漆废气处理系统》,申请公布号:CN 105289156 A,公开的喷漆室废气处理系统的处理效果不理想,对喷漆产生的粉尘或漆渣的过滤效果不佳,容易对后续设备造成堵塞,运营成本较高。For example, the Chinese patent "Painting Exhaust Gas Treatment System", application publication number: CN 105289156 A, the treatment effect of the disclosed exhaust gas treatment system in the spray booth is not ideal, and the filtering effect on the dust or paint residue generated by spray painting is not good, and it is easy to cause damage to subsequent equipment. Congestion, higher operating costs.

因此,需要开发一种低成本、高效、易维护的废气处理技术。Therefore, it is necessary to develop a low-cost, high-efficiency, and easy-to-maintain waste gas treatment technology.

为了克服上述缺陷,本领域技术人员积极创新研究,以期创设出一种喷漆室有机废气处理系统。In order to overcome the above-mentioned defects, those skilled in the art actively conduct innovative research in order to create a system for treating organic waste gas in a spray booth.

实用新型内容Utility model content

针对现有技术存在的问题,本实用新型提供了一种喷漆室有机废气处理系统,解决了喷漆废气易堵塞、废气不能稳定达标的问题,且系统的自动化和智能化程度高,对废气的处理效果佳,净化效率>98%,满足并高于国家排放标准;且能够在线对废气催化燃烧处理,实现废气的零排放。Aiming at the problems existing in the prior art, the utility model provides a treatment system for organic waste gas in the spray booth, which solves the problems that the waste gas from spray painting is easy to block and the waste gas cannot reach the standard stably. The effect is good, the purification efficiency is >98%, which meets and exceeds the national emission standard; and it can process the exhaust gas catalytic combustion online to achieve zero emission of exhaust gas.

为解决上述技术问题,本实用新型采用的一个技术方案是:提供一种喷漆室有机废气处理系统,包括干式过滤器、吸附脱附箱、催化燃烧装置、吸附风机、脱附风机和补气风机,所述吸附脱附箱设有三个,每一所述吸附脱附箱皆具有吸附进气口、吸附出气口、脱附进气口和脱附出气口,所述干式过滤器的进气口连接废气收集管道,所述干式过滤器的出气口与吸附脱附箱的吸附进气口通过吸附进气管道连接,所述吸附脱附箱的吸附出气口与吸附风机通过吸附出气管道连接,所述吸附风机的出风口连接排气烟囱;所述吸附脱附箱的脱附出气口与所述催化燃烧装置通过脱附出气管道连接,所述催化燃烧装置与所述吸附脱附箱的脱附进气口通过回风管道连接,所述回风管道包括第一回风管道和第二回风管道,所述第一回风管道设有脱附风机,第一回风管道同时与第二回风管道和排风管道连接;所述补气风机设于补气管道,所述补气管道的一端与空气连通,另一端与脱附出气管道连接;In order to solve the above technical problems, a technical solution adopted by the utility model is to provide a treatment system for organic waste gas in a spray booth, including a dry filter, an adsorption and desorption box, a catalytic combustion device, an adsorption fan, a desorption fan and an air supplement fan, the adsorption-desorption box is provided with three, and each of the adsorption-desorption boxes has an adsorption air inlet, an adsorption air outlet, a desorption air inlet and a desorption air outlet, and the inlet of the dry filter The air port is connected to the exhaust gas collection pipeline, the air outlet of the dry filter is connected to the adsorption air inlet of the adsorption desorption box through the adsorption air intake pipeline, and the adsorption air outlet of the adsorption desorption box is connected to the adsorption fan through the adsorption air outlet pipeline connected, the air outlet of the adsorption fan is connected to the exhaust chimney; the desorption outlet of the adsorption and desorption box is connected with the catalytic combustion device through a desorption outlet pipeline, and the catalytic combustion device is connected with the adsorption and desorption box The desorption air inlet is connected by a return air duct, the return air duct includes a first return air duct and a second return air duct, the first return air duct is provided with a desorption fan, and the first return air duct is simultaneously connected with the The second return air duct is connected to the exhaust duct; the air supply fan is arranged on the air supply pipeline, one end of the air supply pipeline communicates with the air, and the other end is connected with the desorption air outlet pipeline;

所述废气收集管道还连接检修管道,所述废气收集管道设有进气阀,所述检修管道设有检修阀,所述吸附进气管道设有吸附进气阀,所述吸附出气管道设有吸附出气阀,所述脱附出气管道设有脱附出气阀,所述第二回风管道设有回风阀,所述排风管道设有排风阀,所述补气管道设有补气阀;The waste gas collection pipeline is also connected to the maintenance pipeline, the waste gas collection pipeline is provided with an intake valve, the maintenance pipeline is provided with a maintenance valve, the adsorption intake pipeline is provided with an adsorption intake valve, and the adsorption outlet pipeline is provided with Adsorption air outlet valve, the desorption air outlet pipeline is provided with a desorption air outlet valve, the second air return pipeline is provided with a return air valve, the exhaust air pipeline is provided with an exhaust valve, and the air supply pipeline is provided with an air supply valve valve;

所述催化燃烧装置内设有预热室、催化床、换热器和第一热电偶,所述预热室内具有加热器;The catalytic combustion device is provided with a preheating chamber, a catalytic bed, a heat exchanger and a first thermocouple, and a heater is provided in the preheating chamber;

所述脱附出气管道且位于所述催化燃烧装置的上游设有阻火除尘器,所述阻火除尘器内具有多层金属网,每层金属网的厚度为1-2mm,所述金属网的网格的长为0.2-0.3mm且宽为0.05-0.1mm;The desorption gas outlet pipeline is located upstream of the catalytic combustion device and is provided with a fire arrester and dust collector. There are multiple layers of metal mesh in the fire arrester and dust collector, and the thickness of each layer of metal mesh is 1-2mm. The metal mesh The length of the grid is 0.2-0.3mm and the width is 0.05-0.1mm;

还包括PLC控制系统,所述PLC控制系统包括PLC控制器、安装于所述吸附脱附箱的第二热电偶以及第一超温报警器、安装于所述催化燃烧装置的第二超温报警器和设于所述干式过滤器的压差计,所述PLC控制器安装于控制柜,所述吸附风机、脱附风机、补气风机、进气阀、检修阀、吸附进气阀、吸附出气阀、脱附出气阀、回风阀、排风阀、补气阀、换热器、第一热电偶、加热器、第二热电偶、第一超温报警器和第二超温报警器皆分别与所述PLC控制器电连接。Also includes a PLC control system, the PLC control system includes a PLC controller, a second thermocouple installed in the adsorption-desorption box, a first over-temperature alarm, and a second over-temperature alarm installed in the catalytic combustion device The device and the differential pressure gauge located on the dry filter, the PLC controller is installed in the control cabinet, the adsorption fan, desorption fan, air supply fan, intake valve, maintenance valve, adsorption intake valve, Adsorption outlet valve, desorption outlet valve, air return valve, exhaust valve, air supply valve, heat exchanger, first thermocouple, heater, second thermocouple, first over-temperature alarm and second over-temperature alarm devices are respectively electrically connected to the PLC controller.

进一步地说,所述吸附风机为具有变频器的变频风机。Furthermore, the adsorption fan is a variable frequency fan with a frequency converter.

进一步地说,所述干式过滤器的滤材为干式填料层和中效过滤层,所述干式填料层位于中效过滤层的上游,所述干式填料层为鲍尔环填料,且所述干式填料层的厚度>500mm,所述中效过滤层包括金属网框和夹于所述金属网框的过滤材料,所述过滤材料为由合成纤维无纺布和铝复合物制成的褶皱状复合滤材。Further, the filter material of the dry filter is a dry packing layer and a medium-efficiency filter layer, the dry packing layer is located upstream of the medium-efficiency filter layer, and the dry packing layer is a Pall ring packing, And the thickness of the dry packing layer>500mm, the medium-efficiency filter layer includes a metal mesh frame and a filter material sandwiched in the metal mesh frame, and the filter material is made of synthetic fiber non-woven fabric and aluminum composite A pleated composite filter material.

进一步地说,所述吸附脱附箱包括火灾应急自动喷淋系统,所述火灾应急自动喷淋系统与所述PLC控制器电连接。Furthermore, the adsorption-desorption box includes a fire emergency automatic sprinkler system, and the fire emergency automatic sprinkler system is electrically connected to the PLC controller.

进一步地说,所述金属网框为采用1.5mm厚的镀锌板制成的网框,所述干式过滤器的外壳是厚度为3mm的钢板制成的外壳。Furthermore, the metal mesh frame is made of galvanized sheet with a thickness of 1.5 mm, and the shell of the dry filter is made of steel plate with a thickness of 3 mm.

进一步地说,所述干式过滤器的压差计的压差设定值为300-350Pa。Further, the differential pressure setting value of the differential pressure gauge of the dry filter is 300-350Pa.

进一步地说,所述吸附脱附箱的外壳是厚度为3mm的钢板制成的外壳,所述吸附进气管道是壁厚为1.2mm的镀锌钢管,所述吸附脱附箱内填充蜂窝状活性炭,且所述蜂窝状活性炭的容重为400-450kg/m3Further, the shell of the adsorption and desorption box is a shell made of a steel plate with a thickness of 3mm, and the adsorption air intake pipe is a galvanized steel pipe with a wall thickness of 1.2mm, and the honeycomb shape is filled in the adsorption and desorption box. activated carbon, and the honeycomb activated carbon has a bulk density of 400-450kg/m 3 .

进一步地说,所述催化燃烧装置具有防爆器,所述防爆器为膜片泄压式防爆器,所述防爆器与所述PLC控制器电连接。Further, the catalytic combustion device has an explosion-proof device, which is a diaphragm pressure relief type explosion-proof device, and the explosion-proof device is electrically connected to the PLC controller.

进一步地说,所述催化燃烧装置的外周具有保温层,所述保温层为 80kg/m3的岩棉保温层,且所述保温层的厚度为100mm;所述第一回风管道和所述脱附出气管道皆是壁厚为1.2mm的碳钢管。Further, the outer periphery of the catalytic combustion device has an insulating layer, the insulating layer is 80kg/m 3 rock wool insulating layer, and the thickness of the insulating layer is 100mm; the first return air duct and the The desorption outlet pipes are all carbon steel pipes with a wall thickness of 1.2mm.

进一步地说,催化燃烧室采用陶瓷蜂窝体的贵金属催化剂。Further, the catalytic combustion chamber adopts the noble metal catalyst of the ceramic honeycomb body.

本实用新型的有益效果是:The beneficial effects of the utility model are:

本实用新型能够解决目前喷漆室有机废气加热催化燃烧再生不完全,及脱附过程必须停线脱附,脱附燃烧温度变化太大以及催化燃烧再生过程事故频发的困扰,使废气燃烧排放品质能满足环保要求,而且大大提高废气的净化效率,并且由于将废气从吸附材料中脱附出来,使吸附材料可以再生循环使用,同时由于催化燃烧时有空气补充控制,使得催化燃烧更充分,更彻底,燃烧温度更稳定,及避免燃烧过量或是缺氧燃烧中断;对废气的处理效果佳,净化效率>98%,满足并高于国家排放标准;The utility model can solve the problem of incomplete heating, catalytic combustion and regeneration of organic waste gas in the paint spraying room, and the desorption process must be stopped for desorption, the desorption combustion temperature changes too much and frequent accidents in the catalytic combustion regeneration process, so that the quality of waste gas combustion and emission can be improved. It can meet the requirements of environmental protection, and greatly improve the purification efficiency of exhaust gas, and because the exhaust gas is desorbed from the adsorption material, the adsorption material can be regenerated and recycled. Thoroughly, the combustion temperature is more stable, and avoid excessive combustion or oxygen-deficient combustion interruption; the treatment effect on exhaust gas is good, the purification efficiency is >98%, which meets and exceeds the national emission standard;

且喷漆室有机废气中具有灰尘、漆渣等颗粒较大的杂质,经干式过滤器初步过滤后,能够滤掉它们,避免喷漆室有机废气直接进入吸附脱附箱,造成其堵塞,减少设备的运行故障率;Moreover, there are impurities with large particles such as dust and paint slag in the organic waste gas of the spray booth. After preliminary filtration by the dry filter, they can be filtered out to prevent the organic waste gas from the spray booth from directly entering the adsorption and desorption box, causing its blockage and reducing equipment. operating failure rate;

本实用新型的吸附脱附箱采用蜂窝状活性炭,其与粒(棒)状相比具有优势的热力学性能,低阻低耗,高吸附率等,极适合于大风量下使用;The adsorption and desorption box of the utility model adopts honeycomb-shaped activated carbon, which has superior thermodynamic properties, low resistance, low consumption, high adsorption rate, etc., and is extremely suitable for use under large air volumes;

本实用新型包括催化燃烧装置,催化燃烧室采用陶瓷蜂窝体的贵金属催化剂,阻力小,用低压风机就可以正常运转,不但耗电少而且噪音低,催化燃烧装置的风量是废气源风量的十分之一,同时加热功率维持时间为1小时左右,节约能源,吸附有机物废气的吸附脱附箱,可用催化燃烧处理废气产生的热量进行脱附再生,脱附后的气体再送催化燃烧室净化,不需要外加能量,运行费用低,节能效果显著。The utility model includes a catalytic combustion device. The catalytic combustion chamber adopts the noble metal catalyst of the ceramic honeycomb body, which has small resistance and can operate normally with a low-pressure fan. It not only consumes less power but also has low noise. One, at the same time, the heating power is maintained for about 1 hour to save energy. The adsorption and desorption box for adsorbing organic waste gas can be desorbed and regenerated with the heat generated by catalytic combustion treatment of waste gas. The desorbed gas is then sent to the catalytic combustion chamber for purification. Additional energy is required, the operating cost is low, and the energy saving effect is remarkable.

上述说明仅是本实用新型技术方案的概述,为了能够更清楚了解本实用新型的技术手段,并可依照说明书的内容予以实施,以下以本实用新型的较佳实施例并配合附图详细说明如后。The above description is only an overview of the technical solution of the utility model. In order to understand the technical means of the utility model more clearly and implement it according to the contents of the specification, the following is a detailed description of the preferred embodiment of the utility model with accompanying drawings. back.

附图说明Description of drawings

图1是本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;

图2是本实用新型的控制原理图;Fig. 2 is the control schematic diagram of the utility model;

附图中各部分标记如下:The parts are marked as follows in the accompanying drawings:

干式过滤器1、吸附脱附箱2、催化燃烧装置3、脱附风机4、吸附风机5、补气风机6、废气收集管道7、吸附进气管道8、吸附出气管道9、排气烟囱 10、脱附出气管道11、回风管道12、第一回风管道13、第二回风管道14、排风管道15、补气管道16、检修管道17、进气阀18、检修阀19、吸附进气阀20、吸附出气阀21、脱附出气阀22、回风阀23、排风阀24、催化床25、换热器26、第一热电偶27、加热器28、PLC控制器29、第二热电偶30、第一超温报警器31、第二超温报警器32、压差计33、控制柜34、补气阀36和阻火除尘器37。Dry filter 1, adsorption and desorption box 2, catalytic combustion device 3, desorption fan 4, adsorption fan 5, air supply fan 6, waste gas collection pipe 7, adsorption inlet pipe 8, adsorption outlet pipe 9, exhaust chimney 10. Desorption outlet pipe 11, return air pipe 12, first return air pipe 13, second return air pipe 14, exhaust pipe 15, air supply pipe 16, inspection pipe 17, intake valve 18, inspection valve 19, Adsorption inlet valve 20, adsorption outlet valve 21, desorption outlet valve 22, return air valve 23, exhaust valve 24, catalytic bed 25, heat exchanger 26, first thermocouple 27, heater 28, PLC controller 29 , The second thermocouple 30, the first over-temperature alarm 31, the second over-temperature alarm 32, the differential pressure gauge 33, the control cabinet 34, the gas supply valve 36 and the fire arrester and dust collector 37.

具体实施方式Detailed ways

以下通过特定的具体实施例说明本实用新型的具体实施方式,本领域技术人员可由本说明书所揭示的内容轻易地了解本实用新型的优点及功效。本实用新型也可以其它不同的方式予以实施,即,在不背离本实用新型所揭示的范畴下,能予不同的修饰与改变。The specific implementation of the present utility model is described below through specific specific examples, and those skilled in the art can easily understand the advantages and effects of the present utility model from the content disclosed in this specification. The utility model can also be implemented in other different ways, that is, various modifications and changes can be made without departing from the scope disclosed in the utility model.

实施例:一种喷漆室有机废气处理系统,如图1和图2所示,包括干式过滤器1、吸附脱附箱2、催化燃烧装置3、吸附风机5、脱附风机4和补气风机6,所述吸附脱附箱设有三个,每一所述吸附脱附箱皆具有吸附进气口、吸附出气口、脱附进气口和脱附出气口,所述干式过滤器的进气口连接废气收集管道7,所述干式过滤器的出气口与吸附脱附箱的吸附进气口通过吸附进气管道8连接,所述吸附脱附箱的吸附出气口与吸附风机通过吸附出气管道9连接,所述吸附风机的出风口连接排气烟囱10;所述吸附脱附箱的脱附出气口与所述催化燃烧装置通过脱附出气管道11连接,所述催化燃烧装置与所述吸附脱附箱的脱附进气口通过回风管道12连接,所述回风管道包括第一回风管道13和第二回风管道14,所述第一回风管道设有脱附风机,第一回风管道同时与第二回风管道和排风管道15连接;所述补气风机设于补气管道16,所述补气管道的一端与空气连通,另一端与脱附出气管道连接;Embodiment: A treatment system for organic waste gas in a spray booth, as shown in Figure 1 and Figure 2, including a dry filter 1, an adsorption and desorption box 2, a catalytic combustion device 3, an adsorption fan 5, a desorption fan 4 and an air supplement Fan 6, the adsorption-desorption box is provided with three, each of the adsorption-desorption boxes has an adsorption air inlet, an adsorption air outlet, a desorption air inlet and a desorption air outlet, and the dry filter The air inlet is connected to the waste gas collection pipeline 7, the air outlet of the dry filter is connected with the adsorption air inlet of the adsorption desorption box through the adsorption air intake pipeline 8, and the adsorption air outlet of the adsorption desorption box is passed through the adsorption fan. The adsorption outlet pipeline 9 is connected, and the air outlet of the adsorption fan is connected with the exhaust chimney 10; the desorption outlet of the adsorption desorption box is connected with the catalytic combustion device through the desorption outlet pipeline 11, and the catalytic combustion device is connected with the exhaust gas outlet. The desorption air inlet of described adsorption-desorption box is connected by return air duct 12, and described return air duct comprises first return air duct 13 and second return air duct 14, and described first return air duct is provided with desorption Fan, the first return air duct is connected with the second return air duct and the exhaust duct 15 at the same time; the air supply fan is located in the air supply duct 16, one end of the air supply duct is communicated with the air, and the other end is connected with the desorption outlet. pipe connection;

所述废气收集管道还连接检修管道17,所述废气收集管道设有进气阀18,所述检修管道设有检修阀19,所述吸附进气管道设有吸附进气阀20,所述吸附出气管道设有吸附出气阀21,所述脱附出气管道设有脱附出气阀22,所述第二回风管道设有回风阀23,所述排风管道设有排风阀24,所述补气管道设有补气阀36;The waste gas collection pipeline is also connected to the maintenance pipeline 17, the waste gas collection pipeline is provided with an intake valve 18, the maintenance pipeline is provided with a maintenance valve 19, and the adsorption intake pipeline is provided with an adsorption intake valve 20, and the adsorption The outlet pipeline is provided with an adsorption outlet valve 21, the desorption outlet pipeline is provided with a desorption outlet valve 22, the second air return pipeline is provided with a return valve 23, and the exhaust pipeline is provided with an exhaust valve 24, so The air supply pipeline is provided with an air supply valve 36;

所述催化燃烧装置内设有预热室、催化床25、换热器26和第一热电偶 27,所述预热室内具有加热器28;Described catalytic combustion device is provided with preheating chamber, catalytic bed 25, heat exchanger 26 and first thermocouple 27, and heater 28 is arranged in described preheating chamber;

所述脱附出气管道且位于所述催化燃烧装置的上游设有阻火除尘器37,所述阻火除尘器内具有多层金属网,每层金属网的厚度为1-2mm,所述金属网的网格的长为0.2-0.3mm且宽为0.05-0.1mm;Described desorption gas outlet pipeline is positioned at the upstream of described catalytic combustion device and is provided with fire arresting dust collector 37, has multi-layer metal mesh in described fire arrester dust collector, and the thickness of every layer of metal mesh is 1-2mm, and described metal The mesh of the net has a length of 0.2-0.3 mm and a width of 0.05-0.1 mm;

还包括PLC控制系统,所述PLC控制系统包括PLC控制器29、安装于所述吸附脱附箱的第二热电偶30以及第一超温报警器31、安装于所述催化燃烧装置的第二超温报警器32和设于所述干式过滤器的压差计33,所述PLC 控制器安装于控制柜34,所述吸附风机、脱附风机、补气风机、进气阀、检修阀、吸附进气阀、吸附出气阀、脱附出气阀、回风阀、排风阀、补气阀、换热器、第一热电偶、加热器、第二热电偶、第一超温报警器和第二超温报警器皆分别与所述PLC控制器电连接。It also includes a PLC control system, the PLC control system includes a PLC controller 29, a second thermocouple 30 installed in the adsorption-desorption box and a first over-temperature alarm 31, a second thermocouple installed in the catalytic combustion device Over-temperature alarm 32 and differential pressure gauge 33 located on the dry filter, the PLC controller is installed in the control cabinet 34, the adsorption fan, desorption fan, air supply fan, intake valve, maintenance valve , adsorption inlet valve, adsorption outlet valve, desorption outlet valve, return air valve, exhaust valve, air supply valve, heat exchanger, first thermocouple, heater, second thermocouple, first over-temperature alarm and the second over-temperature alarm are respectively electrically connected to the PLC controller.

所述吸附风机为具有变频器的变频风机。The adsorption fan is a variable frequency fan with a frequency converter.

所述干式过滤器的滤材为干式填料层和中效过滤层,所述干式填料层位于中效过滤层的上游,所述干式填料层为鲍尔环填料,且所述干式填料层的厚度>500mm,所述中效过滤层包括金属网框和夹于所述金属网框的过滤材料,所述过滤材料为由合成纤维无纺布和铝复合物制成的褶皱状复合滤材。The filter material of the dry filter is a dry packing layer and a medium-efficiency filter layer, the dry packing layer is located upstream of the medium-efficiency filter layer, the dry packing layer is a Pall ring packing, and the dry The thickness of the packing layer is >500mm. The medium-efficiency filter layer includes a metal mesh frame and a filter material sandwiched in the metal mesh frame. Composite filter.

所述吸附脱附箱包括火灾应急自动喷淋系统,所述火灾应急自动喷淋系统与所述PLC控制器电连接。The adsorption-desorption box includes a fire emergency automatic sprinkler system, and the fire emergency automatic sprinkler system is electrically connected to the PLC controller.

所述金属网框为采用1.5mm厚的镀锌板制成的网框,所述干式过滤器的外壳是厚度为3mm的钢板制成的外壳。The metal screen frame is a screen frame made of galvanized sheet with a thickness of 1.5 mm, and the shell of the dry filter is a shell made of a steel plate with a thickness of 3 mm.

所述干式过滤器的压差计的压差设定值为300-350Pa。The differential pressure setting value of the differential pressure gauge of the dry filter is 300-350Pa.

所述吸附脱附箱的外壳是厚度为3mm的钢板制成的外壳,所述吸附进气管道是壁厚为1.2mm的镀锌钢管,所述吸附脱附箱内填充蜂窝状活性炭,且所述蜂窝状活性炭的容重为400-450kg/m3The shell of the adsorption-desorption box is a shell made of a steel plate with a thickness of 3mm, and the adsorption air intake pipeline is a galvanized steel pipe with a wall thickness of 1.2mm, and honeycomb activated carbon is filled in the adsorption-desorption box, and the The bulk density of the honeycomb activated carbon is 400-450kg/m 3 .

所述催化燃烧装置具有防爆器,所述防爆器为膜片泄压式防爆器,所述防爆器与所述PLC控制器电连接。The catalytic combustion device has an explosion-proof device, which is a diaphragm pressure relief type explosion-proof device, and the explosion-proof device is electrically connected to the PLC controller.

所述催化燃烧装置的外周具有保温层,所述保温层为80kg/m3的岩棉保温层,且所述保温层的厚度为100mm;所述第一回风管道和所述脱附出气管道皆是壁厚为1.2mm的碳钢管The outer periphery of described catalytic combustion device has thermal insulation layer, and described thermal insulation layer is the rock wool thermal insulation layer of 80kg/ m , and the thickness of described thermal insulation layer is 100mm; All are carbon steel pipes with a wall thickness of 1.2mm

本实施例中,三个所述的吸附脱附箱,其中两个所述的吸附脱附箱处于吸附过程,且一个所述的吸附脱附箱处于脱附过程。In this embodiment, among the three adsorption-desorption boxes, two of the adsorption-desorption boxes are in the adsorption process, and one of the adsorption-desorption boxes is in the desorption process.

本实施例中,所述的喷漆室有机废气处理系统的废气处理量为每小时 3000立方米,所述催化燃烧装置的预热温度为220-250℃,所述脱附风机在负压下工作,所述加热器的功率为48kW,所述吸附风机的功率为37kW。In this embodiment, the waste gas treatment capacity of the organic waste gas treatment system in the spray booth is 3000 cubic meters per hour, the preheating temperature of the catalytic combustion device is 220-250°C, and the desorption fan works under negative pressure , the power of the heater is 48kW, and the power of the adsorption fan is 37kW.

本实施例中,所述排气烟囱为降噪烟囱。In this embodiment, the exhaust chimney is a noise reduction chimney.

本实用新型的工作过程和工作原理如下:Working process and working principle of the present utility model are as follows:

在PLC控制系统的控制下,喷漆室产生的有机废气在吸附风机的牵引下,通过废气收集管道进入干式过滤器,滤掉大的灰尘、颗粒和漆渣等杂质,之后经吸附进气管道,进入吸附脱附箱进行废气中苯等有机挥发气体的吸附,然后经过吸附出气管道和排放烟囱达标排放,此过程中,吸附进气阀和吸附出气阀打开,回风阀和脱附出气阀关闭;Under the control of the PLC control system, the organic waste gas generated in the spray booth is drawn by the adsorption fan and enters the dry filter through the waste gas collection pipe to filter out impurities such as large dust, particles and paint slag, and then passes through the adsorption air intake pipe , enter the adsorption and desorption box for the adsorption of benzene and other organic volatile gases in the waste gas, and then discharge through the adsorption outlet pipe and discharge chimney up to the standard. During this process, the adsorption inlet valve and the adsorption outlet valve are opened, the return air valve and the desorption outlet valve closure;

设有三个吸附脱附箱,其中的两个进行上述的吸附过程,还有一个在PLC 控制系统的控制下,进行气体的脱附过程,对吸附脱附箱的进出口阀门进行切换控制,脱附与吸附互为连锁,使脱附与吸附分别动作,相较于传统的只具有一个吸附箱体的治理装置,需要吸附完成后停线再进行脱附净化,效率高,效果好;There are three adsorption-desorption boxes, two of which carry out the above-mentioned adsorption process, and the other one carries out the gas desorption process under the control of the PLC control system, and switches and controls the inlet and outlet valves of the adsorption-desorption box. Attachment and adsorption are interlocking, so that desorption and adsorption operate separately. Compared with the traditional treatment device with only one adsorption box, it needs to stop the line after the adsorption is completed and then perform desorption and purification. The efficiency is high and the effect is good;

吸附脱附箱的脱附过程为,在PLC控制系统的控制下,吸附进气阀和吸附出气阀关闭,回风阀和脱附出气阀打开,脱附气体通过回风管道进入吸附脱附箱,对吸附的苯等有机物进行脱附,脱附后的气体经脱附出气管道进入催化燃烧装置,将脱附气体催化燃烧达标后经第一回风管道和第二回风管道继续进行脱附,在气温过高时,可以经排风阀和排风管道排放;且在催化燃烧的过程中,若燃烧不充分,可以在补气风机的作用下经补气管道向催化燃烧装置内补入空气,通过控制燃烧所需空气,控制燃烧温度,控制燃烧的稳定性,使脱附气体在催化燃烧床里均匀持续的充分催化燃烧;The desorption process of the adsorption and desorption box is that under the control of the PLC control system, the adsorption inlet valve and the adsorption outlet valve are closed, the return air valve and the desorption outlet valve are opened, and the desorption gas enters the adsorption and desorption box through the return air pipe. , to desorb the adsorbed benzene and other organic substances, the desorbed gas enters the catalytic combustion device through the desorption outlet pipe, and after the desorbed gas is catalytically burned to the standard, the desorption continues through the first return air duct and the second return air duct , when the temperature is too high, it can be discharged through the exhaust valve and exhaust pipe; and in the process of catalytic combustion, if the combustion is not sufficient, it can be replenished into the catalytic combustion device through the air supply pipeline under the action of the air supply fan. Air, by controlling the air required for combustion, controlling the combustion temperature, and controlling the stability of combustion, so that the desorbed gas can be evenly and continuously fully catalytically combusted in the catalytic combustion bed;

且脱附过程中,当吸附脱附箱内的温度过高时,在PLC控制系统的控制下,自动启用火灾应急自动喷淋系统,保证系统的安全、正常进行。And during the desorption process, when the temperature in the adsorption and desorption box is too high, under the control of the PLC control system, the fire emergency automatic sprinkler system is automatically activated to ensure the safety and normal operation of the system.

以上所述仅为本实用新型的实施例,并非因此以上所述仅为本实用新型的实施例,并非因此限制本实用新型的专利范围,凡是利用本实用新型说明书及附图内容所作的等效结构,或直接或间接运用在其他相关的技术领域,均同理包括在本实用新型的专利保护范围内。The above description is only an embodiment of the present utility model, not therefore the above description is only an embodiment of the present utility model, and therefore does not limit the scope of patents of the present utility model. structure, or directly or indirectly used in other related technical fields, are all included in the patent protection scope of the utility model in the same way.

Claims (9)

1. a kind of paint spray booth's organic waste gas treatment system, it is characterised in that:Including dry filter (1), adsorption/desorption case (2), Catalytic combustion system (3), absorption blower (5), desorption blower (4) and tonifying Qi blower (6), there are three the adsorption/desorption case is set, Each adsorption/desorption case all has absorption air inlet, absorption gas outlet, desorption air inlet and desorption gas outlet, the dry type The air inlet of filter connects gas sampling pipeline (7), the absorption of the gas outlet of the dry filter and adsorption/desorption case into Port passes through absorption outlet by absorption admission line (8) connection, the absorption gas outlet of the adsorption/desorption case and absorption blower The air outlet of pipeline (9) connection, the absorption blower connects exhaust chimney (10);The desorption gas outlet of the adsorption/desorption case with For the catalytic combustion system by desorption outlet pipe (11) connection, the catalytic combustion system is de- with the adsorption/desorption case Attached air inlet is connected by return air duct (12), and the return air duct includes the first return air duct (13) and the second return air duct (14), first return air duct be equipped with desorption blower, the first return air duct simultaneously with the second return air duct and exhaust duct (15) it connects;The tonifying Qi blower is set to tonifying Qi pipeline (16), one end of the tonifying Qi pipeline and air communication, the other end and de- Attached outlet pipe connection;
The gas sampling pipeline is also connected with service conduits (17), and the gas sampling pipeline is equipped with intake valve (18), the inspection Pipeline is repaired equipped with service valve (19), the absorption admission line is equipped with absorption intake valve (20), and the absorption outlet pipe is equipped with Adsorption outlet valve (21), the desorption outlet pipe are equipped with desorption air outlet valve (22), and second return air duct is equipped with air returning valve (23), the exhaust duct is equipped with exhaust valve (24), and the tonifying Qi pipeline is equipped with aeration valve (36);
Preheating chamber, catalytic bed (25), heat exchanger (26) and the first thermocouple (27) are equipped in the catalytic combustion system, it is described pre- There are heater (28) in hot cell;
The upstream that outlet pipe is desorbed and is located at the catalytic combustion system is equipped with back-fire relief deduster (37), and the back-fire relief removes There is in dirt device multiple layer metal net, every layer of metal mesh with a thickness of 1-2mm, a length of 0.2-0.3mm of the grid of the metal mesh And width is 0.05-0.1mm;
It further include PLC control system, the PLC control system includes PLC controller (29), is installed on the adsorption/desorption case Second thermocouple (30) and the first overtemperature alarm (31), the second overtemperature alarm for being installed on the catalytic combustion system (32) and set on the dry filter differential manometer (33), the PLC controller is installed on control cabinet (34), the absorption wind Machine, desorption blower, tonifying Qi blower, intake valve, service valve, absorption intake valve, adsorption outlet valve, desorption air outlet valve, air returning valve, row Air-valve, aeration valve, heat exchanger, the first thermocouple, heater, the second thermocouple, the first overtemperature alarm and the second overtemperature alarm Device is all electrically connected with the PLC controller respectively.
2. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The absorption blower be with The frequency conversion fan of frequency converter.
3. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The filter of the dry filter Material is dry filler layer and medium air filtration layer, and the dry filler layer is located at the upstream of medium air filtration layer, the dry filler layer For Pall ring filler, and the thickness of the dry filler layer>500mm, the medium air filtration layer include metal screen frame and are sandwiched in institute The filtering material of metal screen frame is stated, the filtering material is that the accordion made of non-woven fabrics of synthetic fiber and aluminium compound is compound Filter material.
4. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The adsorption/desorption case includes Fire disaster emergency automatic sprinkler fire-extinguishing system, the fire disaster emergency automatic sprinkler fire-extinguishing system are electrically connected with the PLC controller.
5. paint spray booth's organic waste gas treatment system according to claim 3, it is characterised in that:The metal screen frame is to use Screen frame made of the galvanized sheet of 1.5mm thickness, the shell of the dry filter are shells made of steel plate with a thickness of 3mm.
6. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The pressure of the dry filter The pressure differential resetting value of difference meter is 300-350Pa.
7. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:Outside the adsorption/desorption case Shell is shell made of steel plate with a thickness of 3mm, and the absorption admission line is the coating steel pipe that wall thickness is 1.2mm, the suction Filled honeycomb shaped activated carbon in attached desorption case, and the bulk density of the Alveolate activated carbon is 400-450kg/m3
8. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The catalytic combustion system tool There is explosion-proof apparatus, the explosion-proof apparatus is diaphragm pressure release type explosion-proof apparatus, and the explosion-proof apparatus is electrically connected with the PLC controller.
9. paint spray booth's organic waste gas treatment system according to claim 1, it is characterised in that:The catalytic combustion system Periphery has insulating layer, and the insulating layer is 80kg/m3Rock wool heat-preservation layer, and the insulating layer with a thickness of 100mm;It is described First return air duct and the desorption outlet pipe are all the carbon steel pipes that wall thickness is 1.2mm.
CN201721911330.1U 2017-12-30 2017-12-30 Paint spray booth's organic waste gas treatment system Expired - Fee Related CN208130662U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107998763A (en) * 2017-12-30 2018-05-08 江苏永益环保科技有限公司 Paint spray booth's organic waste gas treatment system
CN109569190A (en) * 2019-01-17 2019-04-05 广东省盛世环保科技有限公司 A kind of concentration-catalytic combustion device all-in-one machine
CN112090275A (en) * 2020-09-29 2020-12-18 江苏永春环境工程有限公司 Flame-proof type catalytic oxidation device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107998763A (en) * 2017-12-30 2018-05-08 江苏永益环保科技有限公司 Paint spray booth's organic waste gas treatment system
CN109569190A (en) * 2019-01-17 2019-04-05 广东省盛世环保科技有限公司 A kind of concentration-catalytic combustion device all-in-one machine
CN112090275A (en) * 2020-09-29 2020-12-18 江苏永春环境工程有限公司 Flame-proof type catalytic oxidation device

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