WO2023193285A1 - Waste gas treatment method and apparatus using same - Google Patents

Waste gas treatment method and apparatus using same Download PDF

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Publication number
WO2023193285A1
WO2023193285A1 PCT/CN2022/086256 CN2022086256W WO2023193285A1 WO 2023193285 A1 WO2023193285 A1 WO 2023193285A1 CN 2022086256 W CN2022086256 W CN 2022086256W WO 2023193285 A1 WO2023193285 A1 WO 2023193285A1
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Prior art keywords
exhaust gas
filter
treatment
processing module
module
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PCT/CN2022/086256
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French (fr)
Chinese (zh)
Inventor
李东
马鹏涛
杨友强
齐文良
李宝森
林锦龙
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金发科技股份有限公司
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Publication of WO2023193285A1 publication Critical patent/WO2023193285A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42Auxiliary equipment or operation thereof
    • B01D46/4263Means for active heating or cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/007Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • B01D53/44Organic components
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Definitions

  • the present invention relates to the technical field of exhaust gas treatment, and in particular to an exhaust gas treatment method and its device.
  • Exhaust gas usually contains harmful substances such as particulate matter and oil mist. These harmful substances have a significant impact on the environment, but are difficult to treat and make it difficult to meet national emission standards.
  • the waste gas composition is very complex and the production of different product types will produce different types of organic waste gas. Since the plastic product manufacturing industry has the characteristics of many production varieties, small batches and high frequency of production changes, the versatility of waste gas treatment equipment is required. High, and the existing exhaust gas treatment devices are expensive, difficult to clean and maintain later, and improper treatment may even lead to secondary pollution.
  • a first aspect of the present invention provides an exhaust gas treatment method, including the following steps:
  • Step S200 Perform fine filtration treatment on the exhaust gas
  • Step S300 Perform oxidation, photolysis and chlorine addition reaction on the exhaust gas
  • Step S400 Re-filter, dry and defoam the exhaust gas.
  • Step S110 Set up a cylindrical first filter
  • Step S120 Transport the exhaust gas into the interior of the first filter from one end of the first filter;
  • Step S130 Set an annular exhaust gas outlet outside the first filter screen.
  • step S100 also includes:
  • Step S140 Transport water to the inner wall of the first filter to cool it.
  • the porous metal mesh plate, metal mesh and non-woven fabric respectively have pore channels, and the diameters of the pore channels of the porous metal mesh plate, metal mesh and non-woven fabric decrease in sequence.
  • Step S210 Set up an ultrasonic cleaning component and a second filter for fine filtration of the exhaust gas
  • Step S220 Use the ultrasonic cleaning component to intermittently clean the second filter.
  • step S220 includes:
  • Step S222 The ultrasonic cleaning component cleans the first area, and the exhaust gas passes through the second area for fine filtration;
  • Step S223 The ultrasonic cleaning component cleans the second area, and the exhaust gas passes through the first area for fine filtration.
  • step S300 includes: performing oxidation, photolysis and chlorine addition reaction on the exhaust gas.
  • step S300 includes:
  • Step S330 Supply the waste gas into the reaction chamber to perform oxidation, photolysis and chlorine addition reactions.
  • step S400 includes:
  • Step S410 Re-filter the exhaust gas
  • Step S420 Perform drying and defoaming treatment on the exhaust gas.
  • the waste gas treatment method according to the embodiment of the present invention has the following beneficial effects:
  • This embodiment is suitable for the treatment of organic waste gas containing particles and complex components, and can be used as a general solution for waste gas treatment.
  • This embodiment has a high degree of integration, low design and construction costs, a small floor area, and high processing efficiency.
  • a second aspect of the present invention provides an exhaust gas treatment device, including a first processing module, a second processing module, a third processing module and a fourth processing module; the first processing module is used to sequentially treat the exhaust gas Cooling treatment and coarse filtration are carried out.
  • the second treatment module is used to finely filter the exhaust gas flowing out from the first treatment module.
  • the third treatment module is used to oxidize and light the exhaust gas flowing out from the second treatment module. Decomposition and chlorine addition reaction, the fourth treatment module is used to re-filter and dry the exhaust gas flowing out from the third treatment module; wherein, the first treatment module, the second treatment module, the The third processing module and the fourth processing module are stacked in sequence.
  • Figure 1 is a flow chart of an exhaust gas treatment method according to an embodiment of the present invention.
  • Figure 2 is an overall structural diagram of the first processing module according to the embodiment of the present invention.
  • Figure 3 is an overall front view of the first processing module according to the embodiment of the present invention.
  • FIG. 4 is a cross-sectional view along the line A-A in FIG. 3 of the first processing module according to the embodiment of the present invention.
  • Figure 5 shows the positional relationship between the first rotating shaft, water pipe, column, scraper and fixed column of the first processing module according to the embodiment of the present invention.
  • Figure 6 is a structural diagram of the second processing module and the second part of the first barrel according to the embodiment of the present invention.
  • Figure 7 is an overall structural diagram of the second processing module according to the embodiment of the present invention.
  • Figure 8 is a front view of the second processing module according to the embodiment of the present invention.
  • Fig. 9 is a cross-sectional view along the B-B direction in Fig. 8 of the second processing module according to the embodiment of the present invention.
  • Figure 10 is an overall structural diagram of the third processing module according to the embodiment of the present invention.
  • Fig. 11 is a cross-sectional view along the C-C direction in Fig. 10 of the third processing module according to the embodiment of the present invention.
  • Figure 12 is another schematic diagram of the third processing module according to the embodiment of the present invention.
  • Figure 13 is an overall structural diagram of the fourth processing module according to the embodiment of the present invention.
  • FIG. 14 is a cross-sectional view along the D-D direction in FIG. 13 of the fourth processing module according to the embodiment of the present invention.
  • Figure 15 is a front view of the fourth processing module according to the embodiment of the present invention.
  • Fig. 16 is an overall cross-sectional view of the exhaust gas treatment device according to the embodiment of the present invention.
  • first processing module 110, base; 111, first air inlet; 120, first cylinder; 121, first part; 122, second part; 130, first filter; 131, cover Plate; 140, first outlet; 150, first rotating shaft; 160, water pipe; 170, column; 180, scraper; 190, fixed column;
  • connection In the present invention, unless otherwise clearly stated and limited, the terms “installation”, “connection”, “connection”, “fixing” and other terms should be understood in a broad sense. For example, it can be a fixed connection or a detachable connection. , or integrated; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be an internal connection between two elements or an interaction between two elements.
  • connection connection
  • fixing and other terms should be understood in a broad sense. For example, it can be a fixed connection or a detachable connection. , or integrated; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be an internal connection between two elements or an interaction between two elements.
  • Step S100 Perform cooling treatment and coarse filtration treatment on the exhaust gas in sequence
  • Step S200 Perform fine filtration treatment on the exhaust gas
  • Step S300 Perform oxidation, photolysis and chlorine addition reaction on the exhaust gas
  • Step S400 Re-filter, dry and defoam the exhaust gas.
  • step S100 the temperature in the exhaust gas is reduced to prevent other parts of the exhaust gas treatment device of this embodiment from being damaged by high temperature, and after rough filtration, large particulate matter in the exhaust gas will be removed; after step S200 , after the exhaust gas is finely filtered, the small particles of dust, oil mist and water vapor in the exhaust gas that have not been removed by coarse filtration are removed; after step S300, the organic matter in the exhaust gas undergoes a chemical reaction and is removed from the gas; after step S400, When the third treatment module 300 performs the reaction, the gas and moisture mixed into the exhaust gas to perform oxidation and chlorine addition reactions on the exhaust gas will be removed, so that the discharged exhaust gas meets the emission standards.
  • the waste gas passes through the first processing module 100, the second processing module 200, the third processing module 300 and the fourth processing module 400 from bottom to top; after passing through the first processing module 100 hours, the temperature in the exhaust gas is lowered to prevent other parts of the exhaust gas treatment device of this embodiment from being damaged by high temperature, and after rough filtration, large particulate matter in the exhaust gas will be removed; after the second processing module 200 When the exhaust gas undergoes fine filtration, the small particles of dust, oil mist and water vapor in the exhaust gas that have not been removed by rough filtration are removed; when passing through the third processing module 300, the organic matter in the exhaust gas undergoes a chemical reaction and is removed from the gas; after When the fourth treatment module 400 is used, the gas and moisture mixed into the exhaust gas to perform oxidation and chlorine addition reactions on the exhaust gas during the reaction in the third treatment module 300 will be removed to facilitate discharge.
  • this embodiment has the following beneficial effects:
  • This embodiment is suitable for the treatment of organic waste gas containing particles and complex components, and can be used as a general solution for waste gas treatment.
  • This embodiment has a high degree of integration, low design and construction costs, a small floor area, and high processing efficiency.
  • the waste gas with complex components described in this embodiment refers to the waste gas containing high-temperature oil mist, dust, halides, and gaseous volatile organic compounds produced by high-temperature cracking (such as aromatics, amines, hydrogen sulfide, phenols, Aldehydes, acids, alkalis, unsaturated hydrocarbons, etc.) organic waste gas.
  • high-temperature cracking such as aromatics, amines, hydrogen sulfide, phenols, Aldehydes, acids, alkalis, unsaturated hydrocarbons, etc.
  • the specific composition of this organic waste gas is related to the type of products that need to be produced.
  • step S100 includes:
  • Step S110 Set up a cylindrical first filter 130
  • Step S120 Transport the exhaust gas into the interior of the first filter 130 from one end of the first filter 130;
  • Step S130 Set an annular exhaust gas outlet outside the first filter 130.
  • the exhaust gas enters the first cylinder 120 from the middle and moves laterally to pass through the first filter 130 to achieve rough filtration.
  • the lateral movement speed is slow, so The filtering effect is good.
  • the exhaust gas enters the first filter screen 130 from the first air inlet 111 and flows in a direction generally parallel to the first filter screen 130. After passing through the first filter screen 130 transversely, it flows from the first outlet 140 outflow.
  • step S100 also includes:
  • the exhaust gas treatment device further includes a first rotating shaft 150 , a plurality of water pipes 160 , a plurality of columns 170 and a plurality of scrapers 180 ;
  • the first rotating shaft 150 is disposed in the first filter screen 130 and extends along the axis of the first filter screen 130 .
  • a plurality of water delivery pipes 160 are respectively arranged at circumferential intervals around the first rotating shaft 150 .
  • the water pipes 160 respectively extend toward the inner wall of the first filter 130 and are close to the inner wall of the first filter 130.
  • the first rotating shaft 150 is hollow inside, and a plurality of the water pipes 160 are connected to the first rotating shaft respectively.
  • a plurality of uprights 170 correspond to a plurality of water pipes 160, and each of the uprights 170 is installed on the end of the corresponding water pipe 160 away from the first rotating shaft 150; a plurality of the The scraper 180 corresponds to the plurality of uprights 170 one by one, and each scraper 180 is installed along the corresponding upright 170 and attached to the inner wall of the first filter 130 .
  • a liquid collecting tank is provided on the base 110, and a waste water outlet is provided at the bottom of the liquid collecting tank; the first air inlet 111 is opened in the middle of the liquid collecting tank.
  • the exhaust gas enters the second cylinder 220 laterally from the second air inlet 221 on the side of the second cylinder 220, stays in the second cylinder 220, then flows upward and passes through second filter screen 230; during this period, when the amount of exhaust gas filtered by the second filter screen 230 reaches a certain value, it is considered that the impurities remaining on the second filter screen 230 will affect the filtering effect of the second filter screen 230, and then the access is opened.
  • the liquid port is used to fill the second cylinder 220 with liquid. When the liquid fills the second cylinder 220, the ultrasonic component is turned on, and the vibrator 240 vibrates to clean the second filter 230.
  • Step S222 The ultrasonic cleaning component cleans the first area, and the exhaust gas passes through the second area for fine filtration;
  • a third rotating shaft 340 is also included.
  • the number of photolysis light sources 330 is multiple and each is in a strip shape.
  • the plurality of photolysis light sources 330 are arranged at circumferential intervals on the third rotating shaft 340 .
  • step S300 includes:
  • Step S330 Supply the waste gas into the reaction chamber 311 to perform oxidation, photolysis and chlorine addition reactions.
  • the first treatment module 100 needs to use liquid to clean the first filter screen 130
  • the second treatment module 200 needs to use liquid to clean the second filter screen 230
  • the third treatment module 300 needs to use liquid to clean the second filter screen 230.
  • Various gases are needed to perform oxidation, photolysis and chlorine addition reactions on the waste gas
  • the fourth treatment module 400 needs liquid to process the filter assembly 420 .
  • the water circulation module 500 includes a water tank 510 , a first water supply pipe 550 connecting the water tank 510 and the liquid inlet pipe 430 , a clean water outlet and a
  • the sewage pool 540 connected to the sewage outlet of the filter box 520, the second water supply pipe 570 connecting the sewage pool 540 and the inside of the first rotating shaft 150, the electrolytic gas outlet and the second cylinder 220.
  • the gas supply pipe 580, and the circulation pipe 590 connecting the electrolytic liquid outlet and the water tank 510.
  • the consumption of electrolyte can be effectively reduced, thereby increasing the service life of the water circulation module 500 and reducing maintenance costs.
  • a pump body is provided to improve the efficiency of water circulation.
  • the pump body has a filtering function to prevent impurities from entering the pump body and damaging the pump body.
  • the pump body is a ceramic membrane pump.

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  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Abstract

A waste gas treatment method and an apparatus using same. The waste gas treatment method comprises the following steps: step S100: sequentially performing cooling treatment and coarse filtration treatment on waste gas; step S200: performing fine filtration on the waste gas; step S300: performing oxidation, photolysis and chlorine addition reactions on the waste gas; and step S400: performing refiltration treatment, and drying and demisting treatment on the waste gas. The solution is suitable for organic waste gas treatment comprising particles and complex components, and can serve as a universal solution for waste gas treatment; moreover, the integration level is high, the design and construction costs are low, the occupied area is small, and the treatment efficiency is high.

Description

一种废气处理方法及其装置Waste gas treatment method and device 技术领域Technical field
本发明涉及废气处理技术领域,特别是涉及一种废气处理方法及其装置。The present invention relates to the technical field of exhaust gas treatment, and in particular to an exhaust gas treatment method and its device.
背景技术Background technique
废气中通常含有颗粒物、油雾等有害物质,这些有害物质对环境造成重大影响,但又难以处理,难以使其达到国家排放标准。Exhaust gas usually contains harmful substances such as particulate matter and oil mist. These harmful substances have a significant impact on the environment, but are difficult to treat and make it difficult to meet national emission standards.
以塑胶行业为例,为赋予塑胶材料特定性能,在生产时需要加入各种填料和助剂,在塑胶的高温加工过程中产生含有高温油雾、粉尘、卤化物以及高温裂解产生含有气态挥发性有机物的有机废气。这些有机废气将产生恶臭,如果不对其进行有效的收集和处理,将严重污染当地周边的生态环境,并对周边地区的居民和企业内的生产员工造成人身伤害。此外,这些废气中的挥发性有机物会部分凝结在管道内壁上,长期运行下,管道内壁将积累较多的这种可燃油垢,给生产带来了安全隐患。处理时,废气成分非常复杂且不同的产品种类的生产将产生不同种类的有机废气,由于塑胶产品制造业具有生产品种多,批量少且转产频率高的特点,对废气处理设备的通用性要求较高,而现有的废气处理装置昂贵,后期的清理和维护工作困难,处理不当甚至还会导致二次污染。Take the plastic industry as an example. In order to give plastic materials specific properties, various fillers and additives need to be added during production. During the high-temperature processing of plastics, high-temperature oil mist, dust, halides and gaseous volatile substances are produced during high-temperature cracking. Organic waste gases from organic matter. These organic waste gases will produce stench. If they are not effectively collected and processed, they will seriously pollute the local ecological environment and cause personal injury to residents in surrounding areas and production employees in enterprises. In addition, the volatile organic compounds in these exhaust gases will partially condense on the inner wall of the pipeline. Under long-term operation, the inner wall of the pipeline will accumulate more combustible oil scale, which brings safety risks to production. During treatment, the waste gas composition is very complex and the production of different product types will produce different types of organic waste gas. Since the plastic product manufacturing industry has the characteristics of many production varieties, small batches and high frequency of production changes, the versatility of waste gas treatment equipment is required. High, and the existing exhaust gas treatment devices are expensive, difficult to clean and maintain later, and improper treatment may even lead to secondary pollution.
目前,现有技术中往往需要定制化相关设备以对成分复杂的废气进行处理,但这种定制化的设备通用性较差,成本较高。At present, the existing technology often requires customized related equipment to process exhaust gas with complex components. However, this customized equipment has poor versatility and high cost.
发明内容Contents of the invention
本发明的目的是:提供一种通用性较好、成本较低且适于对成分复杂的废气进行处理的废气处理方法,及应用该废气处理方法处理废气的废气处理装置。The object of the present invention is to provide an exhaust gas treatment method with good versatility, low cost and suitable for treating exhaust gas with complex components, and an exhaust gas treatment device that uses the exhaust gas treatment method to treat exhaust gas.
为了实现上述目的,本发明第一方面提供了一种废气处理方法,包括如下步骤:In order to achieve the above objects, a first aspect of the present invention provides an exhaust gas treatment method, including the following steps:
步骤S100:对废气依次进行降温处理和粗过滤处理;Step S100: Perform cooling treatment and coarse filtration treatment on the exhaust gas in sequence;
步骤S200:对废气进行精过滤处理;Step S200: Perform fine filtration treatment on the exhaust gas;
步骤S300:对废气进行氧化、光解以及氯加成反应;Step S300: Perform oxidation, photolysis and chlorine addition reaction on the exhaust gas;
步骤S400:对废气进行再过滤和干燥除沫处理。Step S400: Re-filter, dry and defoam the exhaust gas.
进一步地,所述步骤S100包括:Further, the step S100 includes:
步骤S110:设置呈筒状的第一过滤网;Step S110: Set up a cylindrical first filter;
步骤S120:将废气从所述第一过滤网的一端输送入所述第一过滤网内部;Step S120: Transport the exhaust gas into the interior of the first filter from one end of the first filter;
步骤S130:在所述第一过滤网外侧设置环形的废气出口。Step S130: Set an annular exhaust gas outlet outside the first filter screen.
进一步地,所述步骤S100还包括:Further, the step S100 also includes:
步骤S140:向所述第一过滤网的内壁输送水以对所述进行降温处理。Step S140: Transport water to the inner wall of the first filter to cool it.
进一步地,步骤S110中设置的第一过滤网包括由内而外依次设置的多孔金属网板、金属丝网以及非织造 布;Further, the first filter screen set in step S110 includes porous metal mesh plates, metal mesh and non-woven fabrics arranged in sequence from the inside to the outside;
所述多孔金属网板、金属丝网以及非织造布分别具有孔道,所述多孔金属网板、金属丝网以及非织造布的孔道直径依次减小。The porous metal mesh plate, metal mesh and non-woven fabric respectively have pore channels, and the diameters of the pore channels of the porous metal mesh plate, metal mesh and non-woven fabric decrease in sequence.
进一步地,所述步骤S200中,所述的对废气进行精过滤处理包括:Further, in step S200, the fine filtration of exhaust gas includes:
步骤S210:设置超声清洗组件和用于对所述废气进行精过滤的第二过滤网;Step S210: Set up an ultrasonic cleaning component and a second filter for fine filtration of the exhaust gas;
步骤S220:利用所述超声清洗组件间歇性清洗所述第二过滤网。Step S220: Use the ultrasonic cleaning component to intermittently clean the second filter.
进一步地,所述步骤S220包括:Further, the step S220 includes:
步骤S221:将第二过滤网划分为第一区域和第二区域;Step S221: Divide the second filter into a first area and a second area;
步骤S222:超声清洗组件对第一区域进行清洗,废气经过第二区域进行精过滤;Step S222: The ultrasonic cleaning component cleans the first area, and the exhaust gas passes through the second area for fine filtration;
步骤S223:超声清洗组件对第二区域进行清洗,废气经过第一区域进行精过滤。Step S223: The ultrasonic cleaning component cleans the second area, and the exhaust gas passes through the first area for fine filtration.
进一步地,所述步骤S300包括:对废气进行氧化、光解以及氯加成反应。Further, the step S300 includes: performing oxidation, photolysis and chlorine addition reaction on the exhaust gas.
进一步地,所述步骤S300包括:Further, the step S300 includes:
步骤S310:设置具有反应腔室的反应基座;Step S310: Set up a reaction base with a reaction chamber;
步骤S320:在所述反应腔室内设置分子筛和用于对分子筛进行再生的再生单元;Step S320: Set up a molecular sieve and a regeneration unit for regenerating the molecular sieve in the reaction chamber;
步骤S330:将废气供入至所述反应腔室内以进行氧化、光解以及氯加成反应。Step S330: Supply the waste gas into the reaction chamber to perform oxidation, photolysis and chlorine addition reactions.
进一步地,所述步骤S400包括:Further, the step S400 includes:
步骤S410:对废气进行再过滤处理;Step S410: Re-filter the exhaust gas;
步骤S420:对废气进行干燥除沫处理。Step S420: Perform drying and defoaming treatment on the exhaust gas.
本发明实施例一种废气处理方法与现有技术相比,其有益效果在于:Compared with the existing technology, the waste gas treatment method according to the embodiment of the present invention has the following beneficial effects:
1、本实施例适用于含颗粒和复杂成分的有机废气处理,能够作为废气处理的通用方案。1. This embodiment is suitable for the treatment of organic waste gas containing particles and complex components, and can be used as a general solution for waste gas treatment.
2、本实施例的集成程度较高,设计和建设的成本较低,占地面积较小,且处理效率高。2. This embodiment has a high degree of integration, low design and construction costs, a small floor area, and high processing efficiency.
为了实现上述目的,本发明第二方面提供了一种废气处理装置,包括第一处理模块、第二处理模块、第三处理模块以及第四处理模块;所述第一处理模块用于对废气依次进行降温处理和粗过滤处理,所述第二处理模块用于对从第一处理模块流出的废气进行精过滤,所述第三处理模块用于对从第二处理模块流出的废气进行氧化、光解以及氯加成反应,所述第四处理模块用于对从第三处理模块流出的废气进行再过滤和干燥除沫处理;其中,所述第一处理模块、所述第二处理模块、所述第三处理模块以及所述第四处理模块依次叠放。In order to achieve the above object, a second aspect of the present invention provides an exhaust gas treatment device, including a first processing module, a second processing module, a third processing module and a fourth processing module; the first processing module is used to sequentially treat the exhaust gas Cooling treatment and coarse filtration are carried out. The second treatment module is used to finely filter the exhaust gas flowing out from the first treatment module. The third treatment module is used to oxidize and light the exhaust gas flowing out from the second treatment module. Decomposition and chlorine addition reaction, the fourth treatment module is used to re-filter and dry the exhaust gas flowing out from the third treatment module; wherein, the first treatment module, the second treatment module, the The third processing module and the fourth processing module are stacked in sequence.
附图说明Description of the drawings
图1是本发明实施例的废气处理方法的流程图。Figure 1 is a flow chart of an exhaust gas treatment method according to an embodiment of the present invention.
图2是本发明实施例的第一处理模块的整体结构图。Figure 2 is an overall structural diagram of the first processing module according to the embodiment of the present invention.
图3是本发明实施例的第一处理模块的整体主视图。Figure 3 is an overall front view of the first processing module according to the embodiment of the present invention.
图4是本发明实施例的第一处理模块的图3中的A-A方向剖视图。FIG. 4 is a cross-sectional view along the line A-A in FIG. 3 of the first processing module according to the embodiment of the present invention.
图5是本发明实施例的第一处理模块的第一转轴、输水管、立柱、刮板以及固定柱之间的位置关系。Figure 5 shows the positional relationship between the first rotating shaft, water pipe, column, scraper and fixed column of the first processing module according to the embodiment of the present invention.
图6是本发明实施例的第二处理模块和第一筒体的第二部分的结构图。Figure 6 is a structural diagram of the second processing module and the second part of the first barrel according to the embodiment of the present invention.
图7是本发明实施例的第二处理模块的整体结构图。Figure 7 is an overall structural diagram of the second processing module according to the embodiment of the present invention.
图8是本发明实施例的第二处理模块的主视图。Figure 8 is a front view of the second processing module according to the embodiment of the present invention.
图9是本发明实施例的第二处理模块的图8中的B-B方向剖视图。Fig. 9 is a cross-sectional view along the B-B direction in Fig. 8 of the second processing module according to the embodiment of the present invention.
图10是本发明实施例的第三处理模块的整体结构图。Figure 10 is an overall structural diagram of the third processing module according to the embodiment of the present invention.
图11是本发明实施例的第三处理模块的图10中的C-C方向剖视图。Fig. 11 is a cross-sectional view along the C-C direction in Fig. 10 of the third processing module according to the embodiment of the present invention.
图12是本发明实施例的第三处理模块的另一种示意图。Figure 12 is another schematic diagram of the third processing module according to the embodiment of the present invention.
图13是本发明实施例的第四处理模块的整体结构图。Figure 13 is an overall structural diagram of the fourth processing module according to the embodiment of the present invention.
图14是本发明实施例的第四处理模块的图13中的D-D方向剖视图。FIG. 14 is a cross-sectional view along the D-D direction in FIG. 13 of the fourth processing module according to the embodiment of the present invention.
图15是本发明实施例的第四处理模块的主视图。Figure 15 is a front view of the fourth processing module according to the embodiment of the present invention.
图16是本发明实施例的废气处理装置的整体剖视图。Fig. 16 is an overall cross-sectional view of the exhaust gas treatment device according to the embodiment of the present invention.
图中,100、第一处理模块;110、底座;111、第一进气口;120、第一筒体;121、第一部分;122、第二部分;130、第一过滤网;131、盖板;140、第一出口;150、第一转轴;160、输水管;170、立柱;180、刮板;190、固定柱;In the figure, 100, first processing module; 110, base; 111, first air inlet; 120, first cylinder; 121, first part; 122, second part; 130, first filter; 131, cover Plate; 140, first outlet; 150, first rotating shaft; 160, water pipe; 170, column; 180, scraper; 190, fixed column;
200、第二处理模块;210、底板;220、第二筒体;221、第二进气口;230、第二过滤网;240、振子;250、第二转轴;260、隔板;200. Second processing module; 210. Bottom plate; 220. Second cylinder; 221. Second air inlet; 230. Second filter; 240. Vibrator; 250. Second rotating shaft; 260. Partition plate;
300、第三处理模块;310、反应基座;311、反应腔室;312、第三进气口;320、分子筛;330、光解光源;340、第三转轴;300. Third processing module; 310. Reaction base; 311. Reaction chamber; 312. Third air inlet; 320. Molecular sieve; 330. Photolysis light source; 340. Third rotating shaft;
400、第四处理模块;410、干燥除沫组件;420、过滤组件;430、进液管;440、出液管;400. The fourth processing module; 410. Drying and defoaming component; 420. Filtration component; 430. Liquid inlet pipe; 440. Liquid outlet pipe;
500、水循环模块;510、水箱;520、过滤箱;530、电解池;540、污水池;550、第一供水管;560、第一回水管;570、第二供水管;580、供气管;590、循环管。500. Water circulation module; 510. Water tank; 520. Filter box; 530. Electrolytic cell; 540. Sewage pool; 550. First water supply pipe; 560. First return water pipe; 570. Second water supply pipe; 580. Gas supply pipe; 590. Circulation pipe.
具体实施方式Detailed ways
下面结合附图和实施例,对本发明的具体实施方式作进一步详细描述。以下实施例用于说明本发明,但不用来限制本发明的范围。Specific implementations of the present invention will be described in further detail below with reference to the accompanying drawings and examples. The following examples are used to illustrate the invention but are not intended to limit the scope of the invention.
在本发明的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”“内”、“外”、“顺时针”、“逆时针”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,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发明的限制。In the description of the present invention, it should be understood that the terms "center", "longitudinal", "transverse", "length", "width", "thickness", "upper", "lower", "front", " The directions or positions indicated by "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise" etc. The relationship is based on the orientation or positional relationship shown in the drawings, which is only for the convenience of describing the present invention and simplifying the description, and 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 It should not be construed as a limitation of the present invention.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本发明的描述中,“多个”的含义是两个或两个以上,除非另有明确具体的限定。In addition, the terms “first” and “second” are used for descriptive purposes only and cannot be understood as indicating or implying relative importance or implicitly indicating the quantity of indicated technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include one or more of these features. In the description of the present invention, "plurality" means two or more than two, unless otherwise explicitly and specifically limited.
在本发明中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于 本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。In the present invention, unless otherwise clearly stated and limited, the terms "installation", "connection", "connection", "fixing" and other terms should be understood in a broad sense. For example, it can be a fixed connection or a detachable connection. , or integrated; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be an internal connection between two elements or an interaction between two elements. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.
在本发明中,除非另有明确的规定和限定,第一特征在第二特征之“上”或之“下”可以包括第一和第二特征直接接触,也可以包括第一和第二特征不是直接接触而是通过它们之间的另外的特征接触。而且,第一特征在第二特征“之上”、“上方”和“上面”包括第一特征在第二特征正上方和斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”包括第一特征在第二特征正下方和斜下方,或仅仅表示第一特征水平高度小于第二特征。In the present invention, unless otherwise expressly provided and limited, the term "above" or "below" a first feature of a second feature may include direct contact between the first and second features, or may also include the first and second features. Not in direct contact but through additional characteristic contact between them. Furthermore, the terms "above", "above" and "above" a first feature on a second feature include the first feature being directly above and diagonally above the second feature, or simply mean that the first feature is higher in level than the second feature. “Below”, “under” and “under” the first feature is the second feature includes the first feature being directly below and diagonally below the second feature, or simply means that the first feature is less horizontally than the second feature.
如图1所示,本发明优选实施例的一种废气处理方法,包括如下步骤:As shown in Figure 1, an exhaust gas treatment method according to the preferred embodiment of the present invention includes the following steps:
步骤S100:对废气依次进行降温处理和粗过滤处理;Step S100: Perform cooling treatment and coarse filtration treatment on the exhaust gas in sequence;
步骤S200:对废气进行精过滤处理;Step S200: Perform fine filtration treatment on the exhaust gas;
步骤S300:对废气进行氧化、光解以及氯加成反应;Step S300: Perform oxidation, photolysis and chlorine addition reaction on the exhaust gas;
步骤S400:对废气进行再过滤和干燥除沫处理。Step S400: Re-filter, dry and defoam the exhaust gas.
经过步骤S100后,废气中的温度得到降低,以避免本实施例的废气处理装置的其它部分受到高温而损坏,且,经过粗过滤后,废气中的大颗粒物质将得以去除;经过步骤S200后,废气经过精过滤后,废气中的未被粗过滤除去的小颗粒粉尘、油雾以及水汽得以去除;经过步骤S300后,废气中的有机物发生化学反应,从气体中去除;经过步骤S400后,在第三处理模块300进行反应时混合进废气中以对废气进行氧化和氯加成反应的气体和水分将得以去除,以使得排出的废气符合排放标准。After step S100, the temperature in the exhaust gas is reduced to prevent other parts of the exhaust gas treatment device of this embodiment from being damaged by high temperature, and after rough filtration, large particulate matter in the exhaust gas will be removed; after step S200 , after the exhaust gas is finely filtered, the small particles of dust, oil mist and water vapor in the exhaust gas that have not been removed by coarse filtration are removed; after step S300, the organic matter in the exhaust gas undergoes a chemical reaction and is removed from the gas; after step S400, When the third treatment module 300 performs the reaction, the gas and moisture mixed into the exhaust gas to perform oxidation and chlorine addition reactions on the exhaust gas will be removed, so that the discharged exhaust gas meets the emission standards.
具体地,请参阅图2至图16,本发明优选实施例还提供一种废气处理装置,用于实现上述废气处理方法。其中的废气处理装置,包括第一处理模块100、第二处理模块200、第三处理模块300以及第四处理模块400;所述第一处理模块100、所述第二处理模块200、所述第三处理模块300以及所述第四处理模块400依次叠放;所述第一处理模块100用于对废气依次进行降温处理和粗过滤处理,所述第二处理模块200用于对从第一处理模块100流出的废气进行精过滤处理,所述第三处理模块300用于对从第二处理模块200流出的废气进行氧化、光解以及氯加成反应,所述第四处理模块400用于对从第三处理模块300流出的废气进行再过滤和干燥除沫处理。Specifically, please refer to Figures 2 to 16. A preferred embodiment of the present invention also provides an exhaust gas treatment device for implementing the above exhaust gas treatment method. The exhaust gas treatment device includes a first processing module 100, a second processing module 200, a third processing module 300 and a fourth processing module 400; the first processing module 100, the second processing module 200, the third The three processing modules 300 and the fourth processing module 400 are stacked in sequence; the first processing module 100 is used to sequentially perform cooling processing and coarse filtration processing of the exhaust gas, and the second processing module 200 is used to perform the first processing The exhaust gas flowing out of the module 100 is subjected to fine filtration treatment. The third processing module 300 is used to perform oxidation, photolysis and chlorine addition reaction on the exhaust gas flowing out from the second processing module 200. The fourth processing module 400 is used to The exhaust gas flowing out from the third treatment module 300 is re-filtered, dried and defoamed.
基于上述方案,本实施例在对废气进行处理时,废气由下而上依次经过第一处理模块100、第二处理模块200、第三处理模块300以及第四处理模块400;经过第一处理模块100时,废气中的温度得到降低,以避免本实施例的废气处理装置的其它部分受到高温而损坏,且,经过粗过滤后,废气中的大颗粒物质将得以去除;经过第二处理模块200时,废气经过精过滤后,废气中的未被粗过滤除去的小颗粒粉尘、油雾以及水汽得以去除;经过第三处理模块300时,废气中的有机物发生化学反应,从气体中去除;经过第四处理模块400时,在第三处理模块300进行反应时混合进废气中以对废气进行氧化和氯加成反应的气体和水分将得以去除,以便于排出。Based on the above solution, when processing waste gas in this embodiment, the waste gas passes through the first processing module 100, the second processing module 200, the third processing module 300 and the fourth processing module 400 from bottom to top; after passing through the first processing module 100 hours, the temperature in the exhaust gas is lowered to prevent other parts of the exhaust gas treatment device of this embodiment from being damaged by high temperature, and after rough filtration, large particulate matter in the exhaust gas will be removed; after the second processing module 200 When the exhaust gas undergoes fine filtration, the small particles of dust, oil mist and water vapor in the exhaust gas that have not been removed by rough filtration are removed; when passing through the third processing module 300, the organic matter in the exhaust gas undergoes a chemical reaction and is removed from the gas; after When the fourth treatment module 400 is used, the gas and moisture mixed into the exhaust gas to perform oxidation and chlorine addition reactions on the exhaust gas during the reaction in the third treatment module 300 will be removed to facilitate discharge.
相比于现有技术,本实施例具有如下有益效果:Compared with the existing technology, this embodiment has the following beneficial effects:
1、本实施例适用于含颗粒和复杂成分的有机废气处理,能够作为废气处理的通用方案。1. This embodiment is suitable for the treatment of organic waste gas containing particles and complex components, and can be used as a general solution for waste gas treatment.
2、本实施例的集成程度较高,设计和建设的成本较低,占地面积较小,且处理效率高。2. This embodiment has a high degree of integration, low design and construction costs, a small floor area, and high processing efficiency.
其中,本实施例所述的带有复杂成分的废气,是指带有含有高温油雾、粉尘、卤化物以及高温裂解产生气态挥发性有机物(如芳香族类、胺、硫化氢、酚类、醛类、酸、碱、不饱和烃类等)的有机废气,这种有机废 气的具体成分与需要生产的产品种类有关。Among them, the waste gas with complex components described in this embodiment refers to the waste gas containing high-temperature oil mist, dust, halides, and gaseous volatile organic compounds produced by high-temperature cracking (such as aromatics, amines, hydrogen sulfide, phenols, Aldehydes, acids, alkalis, unsaturated hydrocarbons, etc.) organic waste gas. The specific composition of this organic waste gas is related to the type of products that need to be produced.
进一步地,在一些实施方式中,所述步骤S100包括:Further, in some embodiments, step S100 includes:
步骤S110:设置呈筒状的第一过滤网130;Step S110: Set up a cylindrical first filter 130;
步骤S120:将废气从所述第一过滤网130的一端输送入所述第一过滤网130内部;Step S120: Transport the exhaust gas into the interior of the first filter 130 from one end of the first filter 130;
步骤S130:在所述第一过滤网130外侧设置环形的废气出口。Step S130: Set an annular exhaust gas outlet outside the first filter 130.
本实施例中,废气从中部进入到第一筒体120内,并横向移动以经过第一过滤网130实现粗过滤,其中,在经过第一过滤网130时,横向移动的速度较慢,因此过滤效果良好。In this embodiment, the exhaust gas enters the first cylinder 120 from the middle and moves laterally to pass through the first filter 130 to achieve rough filtration. When passing through the first filter 130, the lateral movement speed is slow, so The filtering effect is good.
在该进一步的实施方式中,为实现上述方法,请参阅图2至图16,废气处理装置中,所述第一处理模块100包括底座110、安装在所述底座110上的第一筒体120和设于所述第一筒体120内的第一过滤网130;所述第一过滤网130围成筒状并与所述第一筒体120同轴设置在所述底座110上;所述底座110具有与所述第一过滤网130内连通的第一进气口111,所述第一筒体120的上边缘和所述第一过滤网130的上边缘之间形成供废气流出的第一出口140。其中,还包括盖板131,盖设在第一过滤网130的上部。In this further embodiment, in order to implement the above method, please refer to Figures 2 to 16. In the exhaust gas treatment device, the first treatment module 100 includes a base 110 and a first cylinder 120 installed on the base 110. and the first filter 130 provided in the first cylinder 120; the first filter 130 is encircled in a cylinder shape and is coaxially arranged with the first cylinder 120 on the base 110; The base 110 has a first air inlet 111 communicated with the first filter 130, and a third air inlet 111 for exhaust gas to flow out is formed between the upper edge of the first cylinder 120 and the upper edge of the first filter 130. 140 for one exit. It also includes a cover plate 131 , which is provided on the upper part of the first filter screen 130 .
上述废气处理装置中,废气由第一进气口111进入到第一过滤网130内,并沿大致平行于第一过滤网130的方向流动,横向经过第一过滤网130后,从第一出口140流出。In the above exhaust gas treatment device, the exhaust gas enters the first filter screen 130 from the first air inlet 111 and flows in a direction generally parallel to the first filter screen 130. After passing through the first filter screen 130 transversely, it flows from the first outlet 140 outflow.
进一步地,在一些实施方式中,所述步骤S100还包括:Further, in some embodiments, step S100 also includes:
步骤S140:向所述第一过滤网130的内壁输送水以对所述进行降温处理。Step S140: Deliver water to the inner wall of the first filter 130 to cool it.
在该进一步的实施方式中,为实现上述方法,请参阅图2至图16,废气处理装置还包括第一转轴150、多个输水管160、多个立柱170以及多个刮板180;所述第一转轴150设置在所述第一过滤网130内并沿所述第一过滤网130的轴线延伸,多个所述输水管160分别绕所述第一转轴150周向间隔设置,多个所述输水管160分别向第一过滤网130的内壁延伸并靠近所述第一过滤网130的内壁,所述第一转轴150内部中空,多个所述输水管160分别连通至所述第一转轴150内部;多个立柱170与多个所述输水管160一一对应,各所述立柱170分别安装在对应的所述输水管160远离所述第一转轴150的端部上;多个所述刮板180与多个所述立柱170一一对应,各所述刮板180分别沿对应的所述立柱170安装并贴设在所述第一过滤网130的内壁上。In this further embodiment, to implement the above method, please refer to FIGS. 2 to 16 , the exhaust gas treatment device further includes a first rotating shaft 150 , a plurality of water pipes 160 , a plurality of columns 170 and a plurality of scrapers 180 ; The first rotating shaft 150 is disposed in the first filter screen 130 and extends along the axis of the first filter screen 130 . A plurality of water delivery pipes 160 are respectively arranged at circumferential intervals around the first rotating shaft 150 . The water pipes 160 respectively extend toward the inner wall of the first filter 130 and are close to the inner wall of the first filter 130. The first rotating shaft 150 is hollow inside, and a plurality of the water pipes 160 are connected to the first rotating shaft respectively. 150 inside; a plurality of uprights 170 correspond to a plurality of water pipes 160, and each of the uprights 170 is installed on the end of the corresponding water pipe 160 away from the first rotating shaft 150; a plurality of the The scraper 180 corresponds to the plurality of uprights 170 one by one, and each scraper 180 is installed along the corresponding upright 170 and attached to the inner wall of the first filter 130 .
上述废气处理装置中,在第一过滤网130过滤的废气量达到一定时,认为此时第一过滤网130上累积的杂质会对第一过滤网130的过滤效果产生较大的影响;此时,第一转轴150工作,多个输水管160、多个立柱170以及多个刮板180随之旋转,其中,多个刮板180贴设着第一过滤网130的内壁转动,能够将第一过滤网130内壁上附着的杂质刮除;同时,多个输水管160内分别通水,水从输水管160的末端流出,沿着刮板180向下流动,以对第一过滤网130的内壁进行清洗;其中,刮板180在进行清理和刮除时,第一过滤网130仍能够正常进行过滤,过滤和清洗互不干扰。In the above exhaust gas treatment device, when the amount of exhaust gas filtered by the first filter 130 reaches a certain level, it is believed that the accumulated impurities on the first filter 130 will have a greater impact on the filtering effect of the first filter 130; at this time, , the first rotating shaft 150 works, and the plurality of water pipes 160, the plurality of columns 170 and the plurality of scrapers 180 rotate accordingly. The plurality of scrapers 180 rotate against the inner wall of the first filter screen 130 and can move the first The impurities attached to the inner wall of the filter screen 130 are scraped off; at the same time, water is passed through the plurality of water pipes 160, and the water flows out from the ends of the water pipes 160 and flows downward along the scraper 180 to clean the inner wall of the first filter screen 130. Carry out cleaning; wherein, when the scraper 180 is cleaning and scraping, the first filter 130 can still filter normally, and filtering and cleaning do not interfere with each other.
其中,在水沿刮板180向下流动时,带走了第一过滤网130上的热量,对第一过滤网130和经过第一过滤网130的废气进行降温。When the water flows downward along the scraper 180 , it takes away the heat on the first filter 130 and cools the first filter 130 and the exhaust gas passing through the first filter 130 .
其中,顺着刮板180向下流动的水将集中在集液槽内,由集液槽收集并集中处理,避免水重新回到本实施方式的工业废水处理装置内。可选地,设置容器,将集液槽内的水集中收集。The water flowing downward along the scraper 180 will be concentrated in the liquid collection tank, where it will be collected and processed centrally to prevent the water from returning to the industrial wastewater treatment device of this embodiment. Optionally, set up a container to centrally collect the water in the collecting tank.
上述实施方式能够实现延长第一处理模块100使用寿命,降低维护成本等有益效果。The above-mentioned embodiments can achieve beneficial effects such as extending the service life of the first processing module 100 and reducing maintenance costs.
优选地,废气处理装置中,所述底座110上设有集液槽,所述集液槽的底部设有废水出口;所述第一进气 口111开设在所述集液槽的中部。Preferably, in the waste gas treatment device, a liquid collecting tank is provided on the base 110, and a waste water outlet is provided at the bottom of the liquid collecting tank; the first air inlet 111 is opened in the middle of the liquid collecting tank.
优选地,废气处理装置中,还包括支架,支架设置在第一转轴150靠近下端上,并分别支撑各个立柱170,以提高立柱170的稳定性。Preferably, the exhaust gas treatment device further includes a bracket, which is disposed near the lower end of the first rotating shaft 150 and supports each upright column 170 to improve the stability of the upright column 170 .
优选地,废气处理装置中,所述第一筒体120由耐腐蚀材料,如不锈钢或带涂层的金属材料或玻璃钢等材料制作形成。Preferably, in the exhaust gas treatment device, the first cylinder 120 is made of corrosion-resistant materials, such as stainless steel, coated metal materials, fiberglass and other materials.
优选地,所述第一转轴150向第一进气口111的方向延伸并穿过第一进气口111;所述第一处理模块100还包括固定柱190,所述固定柱190的数量为多个,多个所述固定柱190沿所述第一转轴150的周向间隔设置在所述第一转轴150穿过所述第一进气口111的端部上,多个所述固定柱190远离所述第一转轴150的端部安装在所述底座110的背面上,以对第一转轴150实现固定。Preferably, the first rotating shaft 150 extends in the direction of the first air inlet 111 and passes through the first air inlet 111; the first processing module 100 further includes fixed columns 190, and the number of the fixed columns 190 is: A plurality of fixed posts 190 are provided at circumferential intervals along the first rotating shaft 150 on the end of the first rotating shaft 150 passing through the first air inlet 111 . The end of 190 away from the first rotating shaft 150 is installed on the back of the base 110 to fix the first rotating shaft 150 .
进一步地,请参阅图2至图16,在一些实施方式中,步骤S110中设置的所述第一过滤网130包括由内而外依次设置的多孔金属网板、金属丝网以及非织造布;所述多孔金属网板、金属丝网以及非织造布分别具有孔道,所述多孔金属网板、金属丝网以及非织造布的孔道直径依次减小。Further, please refer to Figures 2 to 16. In some embodiments, the first filter 130 set in step S110 includes a porous metal mesh plate, a metal mesh and a non-woven fabric arranged in sequence from the inside to the outside; The porous metal mesh plate, metal mesh and non-woven fabric respectively have pore channels, and the diameters of the pore channels of the porous metal mesh plate, metal mesh and non-woven fabric decrease in sequence.
本实施方式中,通过多层设计的结构,第一过滤网130能够实现良好的过滤功能,特别是能够有效地隔绝油污和粉尘。In this embodiment, through the multi-layer design structure, the first filter 130 can achieve a good filtering function, and in particular can effectively isolate oil dirt and dust.
进一步地,在一些实施方式中,所述步骤S200包括:Further, in some embodiments, step S200 includes:
步骤S210:设置超声清洗组件和用于对所述废气进行精过滤的第二过滤网230;Step S210: Set up an ultrasonic cleaning component and a second filter 230 for fine filtration of the exhaust gas;
步骤S220:利用所述超声清洗组件间歇性清洗所述第二过滤网230。Step S220: Use the ultrasonic cleaning component to intermittently clean the second filter 230.
在该进一步的实施方式中,为实现上述方法,废气处理装置中,请参阅图2至图16,所述第二处理模块200包括底板210、设于所述底板210上的第二筒体220、第二过滤网230,以及超声清洗组件;所述第二过滤网230设于所述第二筒体220的顶部并封闭所述第二筒体220顶部的开口,所述超声组件具有设于所述底板210上且处于所述第二筒体220内的振子240,所述第二筒体220的侧面上设有第二进气口221和进液口。In this further embodiment, in order to implement the above method, in the exhaust gas treatment device, please refer to FIGS. 2 to 16 , the second treatment module 200 includes a bottom plate 210 and a second cylinder 220 provided on the bottom plate 210 , a second filter 230, and an ultrasonic cleaning component; the second filter 230 is located on the top of the second cylinder 220 and closes the opening on the top of the second cylinder 220, and the ultrasonic component has a The vibrator 240 is on the bottom plate 210 and is located in the second cylinder 220. A second air inlet 221 and a liquid inlet are provided on the side of the second cylinder 220.
本实施方式中,在进行精滤时,废气从第二筒体220侧面的第二进气口221沿横向进入到第二筒体220内,在第二筒体220内停留后向上流动并经过第二过滤网230;期间,当第二过滤网230过滤的废气量达到一定值时,认为此时第二过滤网230上残留的杂质将影响到第二过滤网230的过滤效果,则打开进液口,向第二筒体220内充入液体,当液体浸满第二筒体220内后,超声组件开启,振子240振动以清洗第二过滤网230。In this embodiment, during fine filtration, the exhaust gas enters the second cylinder 220 laterally from the second air inlet 221 on the side of the second cylinder 220, stays in the second cylinder 220, then flows upward and passes through second filter screen 230; during this period, when the amount of exhaust gas filtered by the second filter screen 230 reaches a certain value, it is considered that the impurities remaining on the second filter screen 230 will affect the filtering effect of the second filter screen 230, and then the access is opened. The liquid port is used to fill the second cylinder 220 with liquid. When the liquid fills the second cylinder 220, the ultrasonic component is turned on, and the vibrator 240 vibrates to clean the second filter 230.
进一步地,在一些实施方式中,所述步骤S220包括:Further, in some implementations, step S220 includes:
步骤S221:将第二过滤网230划分为第一区域和第二区域;Step S221: Divide the second filter 230 into a first area and a second area;
步骤S222:超声清洗组件对第一区域进行清洗,废气经过第二区域进行精过滤;Step S222: The ultrasonic cleaning component cleans the first area, and the exhaust gas passes through the second area for fine filtration;
步骤S223:超声清洗组件对第二区域进行清洗,废气经过第一区域进行精过滤。Step S223: The ultrasonic cleaning component cleans the second area, and the exhaust gas passes through the first area for fine filtration.
在该进一步的实施方式中,为实现上述方法,废气处理装置中,请参阅图2至图16,所述第二处理模块200还包括设于所述第二筒体220内并竖直设置的隔板260;所述隔板260转动设置在所述底板210上,所述隔板260的转轴与所述第二筒体220的轴线重合;所述隔板260将所述第二筒体220分隔为第一区域和第二区域,所述振子240分布在所述第一区域和第二区域内;所述隔板260能够在第一位置和第二位置之间转动切换,当所述隔板260处于所述第一位置上时,所述第一区域与所述第二进气口221连通,所述第二区域与所述进液口连通;当所述隔板260处于所述第二位置上时,所述第二区域与所述第二进气口221连通,所述第一区域与 所述进液口连通。In this further embodiment, in order to implement the above method, in the exhaust gas treatment device, please refer to FIGS. 2 to 16 , the second treatment module 200 further includes a second treatment module 200 disposed vertically in the second cylinder 220 . Partition plate 260; the partition plate 260 is rotatably arranged on the bottom plate 210, and the rotation axis of the partition plate 260 coincides with the axis of the second cylinder 220; the partition plate 260 connects the second cylinder 220 It is divided into a first area and a second area, and the vibrators 240 are distributed in the first area and the second area; the partition 260 can rotate and switch between the first position and the second position. When the partition When the plate 260 is in the first position, the first area is connected to the second air inlet 221, and the second area is connected to the liquid inlet; when the partition plate 260 is in the third When in the second position, the second area is connected to the second air inlet 221, and the first area is connected to the liquid inlet.
本实施方式中,第二处理模块200进行工作时,隔板260处于第一位置上,废气经第二进气口221进入到第一区域内,在第一区域内的第二过滤网230处过滤,当第一区域内的第二过滤网230过滤的废气量一定时,认为此时第一区域内的第二过滤网230上残留的杂质将影响过滤效果,此时隔板260旋转至第二位置,废气经第二进气口221进入到第二区域内,在第二区域内的第二过滤网230处进行过滤;而第一区域将经由进液口进水,处于第一区域内的振子240工作,以对第一区域内的第二过滤网230进行清洗;由此反复,其中一个区域实现对废气的过滤,而同时另一个区域中的第二过滤网230得以清理,清理和过滤同时进行,互不干扰,能够有效地延长第二处理模块200的使用寿命,降低维护成本。In this embodiment, when the second processing module 200 is working, the partition 260 is in the first position, the exhaust gas enters the first area through the second air inlet 221, and the second filter screen 230 in the first area Filtration, when the amount of exhaust gas filtered by the second filter 230 in the first area is constant, it is considered that the remaining impurities on the second filter 230 in the first area will affect the filtering effect. At this time, the partition 260 rotates to the third In the second position, the exhaust gas enters the second area through the second air inlet 221 and is filtered at the second filter 230 in the second area; while the first area will enter water through the liquid inlet and is in the first area. The vibrator 240 works to clean the second filter screen 230 in the first area; thus repeatedly, one area realizes the filtration of the exhaust gas, while at the same time the second filter screen 230 in the other area is cleaned, cleaned and The filtration is performed simultaneously without interfering with each other, which can effectively extend the service life of the second processing module 200 and reduce maintenance costs.
优选地,底板210套设在所述第二筒体220内部,第一筒体120向上延伸至第二筒体220外侧,废气经过第二筒体220和第一筒体120之间的间隙流动至第二进气口221处。可选地,第一筒体120分为与第一过滤网130对应的第一部分121和与所述第二筒体220对应的第二部分122,第一部分121与第二部分122之间通过法兰连接。废气经过第二部分122和第二筒体220之间的间隙,进入第二进气口221内。Preferably, the bottom plate 210 is set inside the second cylinder 220, the first cylinder 120 extends upward to the outside of the second cylinder 220, and the exhaust gas flows through the gap between the second cylinder 220 and the first cylinder 120. to the second air inlet 221. Optionally, the first cylinder 120 is divided into a first part 121 corresponding to the first filter 130 and a second part 122 corresponding to the second cylinder 220. There is a method between the first part 121 and the second part 122. Lan connection. The exhaust gas passes through the gap between the second part 122 and the second cylinder 220 and enters the second air inlet 221 .
优选地,第二过滤网230包括依次叠放的多孔网板和透气滤材;透气滤材具有疏水疏油的功能。可选地,透气滤材为表面进行PTFE处理的非织造PE材料。Preferably, the second filter 230 includes porous mesh plates and breathable filter materials stacked in sequence; the breathable filter material has a hydrophobic and oleophobic function. Optionally, the breathable filter material is a non-woven PE material with a PTFE-treated surface.
优选地,底板210上设有与底板210围成围堰的环体,振子240设置在围堰内。进一步地,从围堰向第一区域或第二区域供水。Preferably, the bottom plate 210 is provided with an annular body that forms a cofferdam with the bottom plate 210 , and the vibrator 240 is disposed in the cofferdam. Further, water is supplied from the cofferdam to the first area or the second area.
优选地,第一区域和第二区域对称设置并分别占据第二筒体220内部空间的一半。Preferably, the first region and the second region are symmetrically arranged and occupy half of the internal space of the second cylinder 220 respectively.
优选地,第二处理模块200还包括第二转轴250,第二转轴250与隔板260连接并能够控制隔板260的转动。可选地,第一转轴150和第二转轴250通过联轴器连接,第一转轴150和第二转轴250同步转动。Preferably, the second processing module 200 further includes a second rotating shaft 250 , which is connected to the partition plate 260 and capable of controlling the rotation of the partition plate 260 . Optionally, the first rotating shaft 150 and the second rotating shaft 250 are connected through a coupling, and the first rotating shaft 150 and the second rotating shaft 250 rotate synchronously.
进一步地,在一些实施方式中,所述步骤S300包括:对废气进行氧化、光解以及氯加成反应。Further, in some embodiments, the step S300 includes: performing oxidation, photolysis and chlorine addition reaction on the exhaust gas.
在该进一步的实施方式中,为实现上述方法,废气处理装置中,请参阅图2至图16,在一些实施方式中,所述第三处理模块300包括反应基座310,所述反应基座310的内部设有用于对废气进行氧化、光解、氯加成的反应腔室311;所述反应基座310的底部具有与所述反应腔室311连通并供废气进入的第三进气口312,所述反应基座310还具有供氧化物质和氯加成物质进入的预定入口;所述第三处理模块300还包括用于照射所述反应腔室311的光解光源330。In this further embodiment, in order to implement the above method, in the exhaust gas treatment device, please refer to Figures 2 to 16. In some embodiments, the third treatment module 300 includes a reaction base 310, and the reaction base The interior of 310 is provided with a reaction chamber 311 for oxidation, photolysis, and chlorine addition of exhaust gas; the bottom of the reaction base 310 has a third air inlet connected to the reaction chamber 311 and for the exhaust gas to enter. 312. The reaction base 310 also has a predetermined entrance for oxidizing substances and chlorine addition substances to enter; the third processing module 300 also includes a photolysis light source 330 for irradiating the reaction chamber 311.
本实施方式,第三处理模块300对废气进行氧化、光解、氯加成等化学处理,同时进行多个化学处理方式,保证能够有效地去除废气中的目标物。In this embodiment, the third processing module 300 performs chemical treatments such as oxidation, photolysis, and chlorine addition on the exhaust gas, and simultaneously performs multiple chemical treatment methods to ensure that target objects in the exhaust gas can be effectively removed.
优选地,在一些实施方式中,第二处理模块200和第三处理模块300之间设有缓冲筒体,所述缓冲筒体内设有缓冲通道,所述第三进气口312与所述缓冲通道的上端连通,所述缓冲通道的下端与所述第二筒体220的上端连通;预定入口连通至第二筒体220内。在本优选实施方式中,可通过将氧化物质和氯加成物质输送至第二筒体220内,使得氧化物质和氯加成物质以及废气能够共同从第二筒体220内流出至缓冲通道内,以在缓冲通道内混合均匀后,再进入到反应腔室311内进行反应,化学处理的反应彻底、高效。Preferably, in some embodiments, a buffer cylinder is provided between the second processing module 200 and the third processing module 300, a buffer channel is provided in the buffer cylinder, and the third air inlet 312 is connected to the buffer cylinder. The upper end of the channel is connected, and the lower end of the buffer channel is connected with the upper end of the second cylinder 220 ; the predetermined entrance is connected to the second cylinder 220 . In this preferred embodiment, oxidizing substances and chlorine adding substances can be transported into the second cylinder 220 so that oxidizing substances, chlorine adding substances and waste gas can flow out from the second cylinder 220 into the buffer channel together. , after mixing evenly in the buffer channel, it then enters the reaction chamber 311 for reaction. The chemical treatment reaction is thorough and efficient.
优选地,光解光源330为UV石英光管。Preferably, the photolysis light source 330 is a UV quartz light pipe.
优选地,还包括第三转轴340,光解光源330的数量为多个且分别呈条形,多个光解光源330呈周向间隔设置在第三转轴340上。Preferably, a third rotating shaft 340 is also included. The number of photolysis light sources 330 is multiple and each is in a strip shape. The plurality of photolysis light sources 330 are arranged at circumferential intervals on the third rotating shaft 340 .
进一步地,在一些实施方式中,所述步骤S300包括:Further, in some embodiments, step S300 includes:
步骤S310:设置具有反应腔室311的反应基座310;Step S310: Set up the reaction base 310 with the reaction chamber 311;
步骤S320:在所述反应腔室311内设置分子筛320和用于对分子筛320进行再生的再生单元;Step S320: Set molecular sieve 320 and a regeneration unit for regenerating molecular sieve 320 in the reaction chamber 311;
步骤S330:将废气供入至所述反应腔室311内以进行氧化、光解以及氯加成反应。Step S330: Supply the waste gas into the reaction chamber 311 to perform oxidation, photolysis and chlorine addition reactions.
在该进一步的实施方式中,为实现上述方法,废气处理装置中,请参阅图2至图16,所述第三处理模块300还包括设于所述反应腔室311内的分子筛320和用于对分子筛320进行再生的再生单元,以延长废气在反应腔室311的滞留时间,延长反应时间,提高杂质去除效果。In this further embodiment, in order to implement the above method, in the exhaust gas treatment device, please refer to FIGS. 2 to 16 , the third treatment module 300 further includes a molecular sieve 320 disposed in the reaction chamber 311 and a The regeneration unit regenerates the molecular sieve 320 to extend the residence time of the waste gas in the reaction chamber 311, extend the reaction time, and improve the impurity removal effect.
进一步地,在一些实施方式中,所述步骤S400包括:Further, in some embodiments, step S400 includes:
步骤S410:对废气进行再过滤处理;Step S410: Re-filter the exhaust gas;
步骤S420:对废气进行干燥除沫处理。Step S420: Perform drying and defoaming treatment on the exhaust gas.
在该进一步的实施方式中,为了实现上述方法,废气处理装置中,请参阅图2至图16,所述第四处理模块400包括干燥除沫组件410和过滤组件420;所述干燥除沫组件410设置在所述过滤组件420上方。本实施方式中,第四处理模块400的过滤组件420将从第三处理模块300流出的废气进行进一步的再过滤以除去其中附着的杂质;而干燥除沫组件410对废气进行干燥除沫处理,洁净废气,以排出符合排放标准的废气。In this further embodiment, in order to implement the above method, in the exhaust gas treatment device, please refer to Figures 2 to 16, the fourth treatment module 400 includes a drying and defoaming component 410 and a filtering component 420; the drying and defoaming component 410 is disposed above the filter assembly 420 . In this embodiment, the filter component 420 of the fourth processing module 400 further re-filters the exhaust gas flowing out of the third processing module 300 to remove attached impurities; and the drying and defoaming component 410 performs drying and defoaming processing on the exhaust gas. Clean exhaust gas to discharge exhaust gas that meets emission standards.
优选地,所述第四处理模块400包括排风组件;排风组件包括风机、管道、检测仪器、循环处理导流管以及电机等。Preferably, the fourth processing module 400 includes an exhaust component; the exhaust component includes a fan, a pipeline, a detection instrument, a circulation treatment guide tube, a motor, etc.
进一步地,请参阅图2至图16,在一些实施方式中,所述第四处理模块400还包括进液管430和出液管440,所述进液管430的出口处于所述过滤组件420和干燥除沫组件410之间,所述进液管430的入口处于所述过滤组件420下方。Further, please refer to Figures 2 to 16. In some embodiments, the fourth processing module 400 also includes a liquid inlet pipe 430 and a liquid outlet pipe 440. The outlet of the liquid inlet pipe 430 is located in the filter assembly 420. Between the drying and defoaming assembly 410 , the inlet of the liquid inlet pipe 430 is located below the filter assembly 420 .
本实施方式中,进液管430流出的液体经过过滤组件420,对过滤组件420进行清理,清理后的液体随着出液管440流出,实现延长过滤组件420的使用寿命,降低维护成本的有益效果。In this embodiment, the liquid flowing out of the liquid inlet pipe 430 passes through the filter assembly 420 to clean the filter assembly 420. The cleaned liquid flows out with the liquid outlet pipe 440, thereby extending the service life of the filter assembly 420 and reducing maintenance costs. Effect.
在上述的工业废水处理装置中,第一处理模块100需要用到液体对第一过滤网130进行清理,第二处理模块200需要用到液体对第二过滤网230进行清理,第三处理模块300需要用到各种气体以对废气进行氧化、光解以及氯加成反应,第四处理模块400需要用到液体对过滤组件420进行处理。对此,为保证第一处理模块100、第二处理模块200、第三处理模块300以及第四处理模块400的正常运行,工业废水处理装置还需要包括水循坏模块500,利用水循坏模块500对第一处理模块100、第二处理模块200以及第四处理模块400进行供水;水循坏模块500包括电解组件,以向第三处理模块300供入各种气体。In the above-mentioned industrial wastewater treatment device, the first treatment module 100 needs to use liquid to clean the first filter screen 130, the second treatment module 200 needs to use liquid to clean the second filter screen 230, and the third treatment module 300 needs to use liquid to clean the second filter screen 230. Various gases are needed to perform oxidation, photolysis and chlorine addition reactions on the waste gas, and the fourth treatment module 400 needs liquid to process the filter assembly 420 . In this regard, in order to ensure the normal operation of the first treatment module 100, the second treatment module 200, the third treatment module 300 and the fourth treatment module 400, the industrial wastewater treatment device also needs to include a water circulation module 500, using the water circulation module 500 supplies water to the first processing module 100, the second processing module 200 and the fourth processing module 400; the water circulation module 500 includes an electrolysis component to supply various gases to the third processing module 300.
具体地,在一些实施方式中,请参阅图2至图16,水循坏模块500包括水箱510、连接所述水箱510和所述进液管430的第一供水管550、具有洁净水出口和污水出口的过滤箱520、连接所述过滤箱520和所述出液管440的第一回水管560、与所述过滤箱520的洁净水出口连接且具有电解气体出口和电解液体出口的电解池530、与所述过滤箱520的污水出口连接的污水池540、连接污水池540和第一转轴150内部的第二供水管570、连接所述电解气体出口和所述第二筒体220内的供气管580,以及连接所述电解液体出口和水箱510的循环管590。Specifically, in some embodiments, please refer to FIGS. 2 to 16 , the water circulation module 500 includes a water tank 510 , a first water supply pipe 550 connecting the water tank 510 and the liquid inlet pipe 430 , a clean water outlet and a The filter box 520 of the sewage outlet, the first return pipe 560 connecting the filter box 520 and the liquid outlet pipe 440, and the electrolytic cell connected to the clean water outlet of the filter box 520 and having an electrolytic gas outlet and an electrolytic liquid outlet. 530. The sewage pool 540 connected to the sewage outlet of the filter box 520, the second water supply pipe 570 connecting the sewage pool 540 and the inside of the first rotating shaft 150, the electrolytic gas outlet and the second cylinder 220. The gas supply pipe 580, and the circulation pipe 590 connecting the electrolytic liquid outlet and the water tank 510.
其中,经过过滤组件420后的电解液虽然带有杂质,过滤组件420中过滤池的是经过多次过滤的废气,因此经过过滤组件420后的电解液的洁净程度仍相对较高,因此经过过滤组件420后的电解液可以经过污水出口 流至第一转轴150内,并用于第一过滤网130的清洗。Among them, although the electrolyte after passing through the filter assembly 420 contains impurities, the filter pool in the filter assembly 420 is exhaust gas that has been filtered multiple times. Therefore, the cleanliness of the electrolyte after passing through the filter assembly 420 is still relatively high. Therefore, after filtering The electrolyte after the assembly 420 can flow into the first rotating shaft 150 through the sewage outlet and be used for cleaning the first filter 130 .
水循坏模块500中的水指的是电解液,电解液采用氯化钠/氯酸钠/次氯酸钠/氢氧化钠等部分盐类和表面活性剂的碱性溶液,以在电解后能够生成能够进行化学处理的物质。The water in the water circulation module 500 refers to the electrolyte. The electrolyte uses an alkaline solution of some salts and surfactants such as sodium chloride/sodium chlorate/sodium hypochlorite/sodium hydroxide, so that it can generate energy after electrolysis. Substances that undergo chemical processing.
本优选实施方式中,通过电解液的循环利用,能够有效地减少电解液的消耗,从而提高水循坏模块500的使用寿命,降低维护成本。In this preferred embodiment, through the recycling of electrolyte, the consumption of electrolyte can be effectively reduced, thereby increasing the service life of the water circulation module 500 and reducing maintenance costs.
优选地,设置有泵体,以便提高水循环的效率。可选地,泵体具有过滤功能,以阻挡杂质进入到泵体内,损坏泵体。可选地,泵体为陶瓷薄膜泵。Preferably, a pump body is provided to improve the efficiency of water circulation. Optionally, the pump body has a filtering function to prevent impurities from entering the pump body and damaging the pump body. Optionally, the pump body is a ceramic membrane pump.
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示意性实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。In the description of this specification, reference to the terms "one embodiment," "some embodiments," "illustrative embodiments," "examples," "specific examples," or "some examples" or the like is intended to be incorporated into the description of the implementation. An example or example describes a specific feature, structure, material, or characteristic that is included in at least one embodiment or example of the invention. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
尽管已经示出和描述了本发明的实施例,本领域的普通技术人员可以理解:在不脱离本发明的原理和宗旨的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, those of ordinary skill in the art will appreciate that various changes, modifications, substitutions and variations can be made to these embodiments without departing from the principles and purposes of the invention. The scope of the invention is defined by the claims and their equivalents.

Claims (9)

  1. 一种废气处理方法,其特征在于,包括如下步骤:An exhaust gas treatment method, characterized in that it includes the following steps:
    步骤S100:对废气依次进行降温处理和粗过滤处理;Step S100: Perform cooling treatment and coarse filtration treatment on the exhaust gas in sequence;
    步骤S200:对废气进行精过滤处理;Step S200: Perform fine filtration treatment on the exhaust gas;
    步骤S300:对废气进行氧化、光解以及氯加成反应;Step S300: Perform oxidation, photolysis and chlorine addition reaction on the exhaust gas;
    步骤S400:对废气进行再过滤和干燥除沫处理。Step S400: Re-filter, dry and defoam the exhaust gas.
  2. 根据权利要求1所述的废气处理方法,其特征在于,所述步骤S100包括:The exhaust gas treatment method according to claim 1, characterized in that the step S100 includes:
    步骤S110:设置呈筒状的第一过滤网;Step S110: Set up a cylindrical first filter;
    步骤S120:将废气从所述第一过滤网的一端输送入所述第一过滤网内部;Step S120: Transport the exhaust gas into the interior of the first filter from one end of the first filter;
    步骤S130:在所述第一过滤网外侧设置环形的废气出口。Step S130: Set an annular exhaust gas outlet outside the first filter screen.
  3. 根据权利要求2所述的废气处理方法,其特征在于,所述步骤S100还包括:The exhaust gas treatment method according to claim 2, characterized in that step S100 further includes:
    步骤S140:向所述第一过滤网的内壁输送水以对所述进行降温处理。Step S140: Transport water to the inner wall of the first filter to cool it.
  4. 根据权利要求2所述的废气处理方法,其特征在于,步骤S110中设置的第一过滤网包括由内而外依次设置的多孔金属网板、金属丝网以及非织造布;The exhaust gas treatment method according to claim 2, characterized in that the first filter screen set in step S110 includes a porous metal mesh plate, a metal mesh and a non-woven fabric arranged in sequence from the inside to the outside;
    所述多孔金属网板、金属丝网以及非织造布分别具有孔道,所述多孔金属网板、金属丝网以及非织造布的孔道直径依次减小。The porous metal mesh plate, metal mesh and non-woven fabric respectively have pore channels, and the diameters of the pore channels of the porous metal mesh plate, metal mesh and non-woven fabric decrease in sequence.
  5. 根据权利要求1所述的废气处理方法,其特征在于,所述步骤S200包括:The exhaust gas treatment method according to claim 1, characterized in that the step S200 includes:
    步骤S210:设置超声清洗组件和用于对所述废气进行精过滤的第二过滤网;Step S210: Set up an ultrasonic cleaning component and a second filter for fine filtration of the exhaust gas;
    步骤S220:利用所述超声清洗组件间歇性清洗所述第二过滤网。Step S220: Use the ultrasonic cleaning component to intermittently clean the second filter.
  6. 根据权利要求5所述的废气处理方法,其特征在于,所述步骤S220包括:The exhaust gas treatment method according to claim 5, characterized in that the step S220 includes:
    步骤S221:将第二过滤网划分为第一区域和第二区域;Step S221: Divide the second filter into a first area and a second area;
    步骤S222:超声清洗组件对第一区域进行清洗,废气经过第二区域进行精过滤;Step S222: The ultrasonic cleaning component cleans the first area, and the exhaust gas passes through the second area for fine filtration;
    步骤S223:超声清洗组件对第二区域进行清洗,废气经过第一区域进行精过滤。Step S223: The ultrasonic cleaning component cleans the second area, and the exhaust gas passes through the first area for fine filtration.
  7. 根据权利要求1所述的废气处理方法,其特征在于,所述步骤S300包括:The exhaust gas treatment method according to claim 1, wherein step S300 includes:
    步骤S310:设置具有反应腔室的反应基座;Step S310: Set up a reaction base with a reaction chamber;
    步骤S320:在所述反应腔室内设置分子筛和用于对分子筛进行再生的再生单元;Step S320: Set up a molecular sieve and a regeneration unit for regenerating the molecular sieve in the reaction chamber;
    步骤S330:将废气供入至所述反应腔室内以进行氧化、光解以及氯加成反应。Step S330: Supply the waste gas into the reaction chamber to perform oxidation, photolysis and chlorine addition reactions.
  8. 根据权利要求1所述的废气处理方法,其特征在于,所述步骤S400包括:The exhaust gas treatment method according to claim 1, wherein step S400 includes:
    步骤S410:对废气进行再过滤处理;Step S410: Re-filter the exhaust gas;
    步骤S420:对废气进行干燥除沫处理。Step S420: Perform drying and defoaming treatment on the exhaust gas.
  9. 一种废气处理装置,其特征在于,包括:An exhaust gas treatment device, characterized by including:
    第一处理模块,所述第一处理模块用于对废气依次进行降温处理和粗过滤处理;A first processing module, the first processing module is used to sequentially perform cooling processing and rough filtration processing on the exhaust gas;
    第二处理模块,所述第二处理模块用于对从第一处理模块流出的废气进行精过滤处理;a second processing module, the second processing module is used to perform fine filtration processing on the exhaust gas flowing out from the first processing module;
    第三处理模块,所述第三处理模块用于对从第二处理模块流出的废气进行氧化、光解以及氯加成反应;以 及A third treatment module, the third treatment module is used for oxidation, photolysis and chlorine addition reaction of the exhaust gas flowing out from the second treatment module; and
    第四处理模块,所述第四处理模块用于对从第三处理模块流出的废气进行再过滤和干燥除沫处理;A fourth treatment module, the fourth treatment module is used to re-filter, dry and defoam the exhaust gas flowing out from the third treatment module;
    其中,所述第一处理模块、所述第二处理模块、所述第三处理模块以及所述第四处理模块依次叠放。Wherein, the first processing module, the second processing module, the third processing module and the fourth processing module are stacked in sequence.
PCT/CN2022/086256 2022-04-06 2022-04-12 Waste gas treatment method and apparatus using same WO2023193285A1 (en)

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