WO2022151699A1 - Combined modular integrated machine for efficient purification of exhaust gas - Google Patents
Combined modular integrated machine for efficient purification of exhaust gas Download PDFInfo
- Publication number
- WO2022151699A1 WO2022151699A1 PCT/CN2021/108327 CN2021108327W WO2022151699A1 WO 2022151699 A1 WO2022151699 A1 WO 2022151699A1 CN 2021108327 W CN2021108327 W CN 2021108327W WO 2022151699 A1 WO2022151699 A1 WO 2022151699A1
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- WO
- WIPO (PCT)
- Prior art keywords
- adsorption
- exhaust gas
- module
- heat exchanger
- air inlet
- Prior art date
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- 238000000746 purification Methods 0.000 title claims abstract description 23
- 238000001179 sorption measurement Methods 0.000 claims abstract description 107
- 238000003795 desorption Methods 0.000 claims abstract description 45
- 238000007084 catalytic combustion reaction Methods 0.000 claims abstract description 40
- 239000000843 powder Substances 0.000 claims abstract description 13
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 239000000463 material Substances 0.000 claims description 17
- 238000009434 installation Methods 0.000 claims description 9
- 238000005507 spraying Methods 0.000 claims description 8
- 239000012855 volatile organic compound Substances 0.000 claims description 8
- 238000007689 inspection Methods 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 4
- 239000002808 molecular sieve Substances 0.000 claims description 4
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 3
- 238000007781 pre-processing Methods 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 claims 1
- 229940098458 powder spray Drugs 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 40
- 239000002245 particle Substances 0.000 abstract description 15
- 239000002918 waste heat Substances 0.000 abstract description 7
- 239000000428 dust Substances 0.000 abstract description 2
- 238000002203 pretreatment Methods 0.000 abstract 2
- 239000003595 mist Substances 0.000 description 14
- 239000003973 paint Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 8
- 239000010815 organic waste Substances 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 239000002956 ash Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000003463 adsorbent Substances 0.000 description 4
- 238000010926 purge Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- FPAFDBFIGPHWGO-UHFFFAOYSA-N dioxosilane;oxomagnesium;hydrate Chemical compound O.[Mg]=O.[Mg]=O.[Mg]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O FPAFDBFIGPHWGO-UHFFFAOYSA-N 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 239000013618 particulate matter Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 206010028400 Mutagenic effect Diseases 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000010882 bottom ash Substances 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000006115 industrial coating Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000243 mutagenic effect Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
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- 239000005416 organic matter Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000007146 photocatalysis Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
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- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 231100000378 teratogenic Toxicity 0.000 description 1
- 230000003390 teratogenic effect Effects 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/02—Separation 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 adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation 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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Definitions
- the invention relates to the technical field of exhaust gas treatment equipment, in particular to a combined modularized high-efficiency exhaust gas purification integrated machine.
- VOCs volatile organic compounds
- the technical problems solved by the present invention are as follows: for the existing activated carbon adsorption, desorption + catalytic combustion process, the front-end particulate matter is not filtered cleanly, it is difficult to replace the filter material, the utilization rate of waste heat is low, the desorption is unstable, the on-site pipeline is complex, and the To solve the problems of large floor area and other problems, a combined modular and efficient exhaust gas purification integrated machine is provided, which has the advantages of compact and simple structure, high purification efficiency, stable desorption and high utilization rate of waste heat, and can effectively remove dust particles and volatilization in the exhaust gas. Sexual organic matter.
- the present invention solves the above-mentioned problems through the following technical means:
- a combined modularized high-efficiency exhaust gas purification integrated machine includes a pretreatment module, an adsorption concentration module, and a power and catalytic combustion module;
- the pretreatment module includes a guide chamber, a powder spraying chamber, and a filter chamber, and the guide chamber has a The side wall is provided with an air inlet, the rear end of the air inlet is provided with a baffle, the top of the dusting chamber is provided with a duster, the filter chamber is provided with a filter cartridge, and the bottom of the filter cartridge is provided with a an ash bucket; an adsorption layer is arranged in the adsorption concentration module;
- the power and catalytic combustion module includes an adsorption fan, a heat exchanger, a catalytic combustion device and a desorption fan, and the adsorption concentration module, the adsorption fan, the heat exchanger, Between the catalytic combustion device and the desorption fan, an integrated unit of adsorption, desorption and catalytic combustion is formed through the matching desorption
- the filter chamber is provided with a backflushing device.
- the two ends of the filter cartridge are provided with pressure sensors, the installation position of the filter cartridge is provided with a pretreatment module inspection door, and the pretreatment module is also equipped with a differential pressure display instrument.
- the adsorption layer includes an adsorption box body and a solid porous adsorption material filled in the adsorption box body, the adsorption box body is drawn and matched with the shell of the adsorption concentration module through the guide rail, and the bottom of the adsorption box body is a mesh plate;
- the adsorbent material is activated carbon or molecular sieve with honeycomb structure.
- the adsorption concentration module is equipped with an adsorption material installation door and a top access door.
- the power and catalytic combustion modules are equipped with fresh air shutters, air outlets and access doors for the power and catalytic combustion modules.
- the air inlet end of the adsorption fan is communicated with the air outlet end of the adsorption concentration module through the air inlet duct, and the air outlet end of the adsorption fan is communicated with the air outlet through the air outlet duct, and the air inlet duct is provided with an adsorption outlet. damper.
- the heat exchanger is provided with the heat exchanger cold air inlet, the heat exchanger hot air outlet, the heat exchanger hot air inlet and the heat exchanger cold air outlet, the heat exchanger cold air inlet and the heat exchanger hot air outlet.
- the hot air inlet of the heat exchanger is communicated with the cold air outlet of the heat exchanger.
- both the air inlet and the air outlet of the catalytic combustion device are provided with flame arresters.
- the air inlet end of the adsorption layer, the interior of the catalytic combustion device and the cold air outlet of the heat exchanger are all provided with temperature detection, and the air outlet of the desorption fan is provided with VOCs concentration detection.
- the concentration of the filtered particles is less than or equal to 1mg/m 3 , and the filter element of the filter cartridge is automatically pulsed backflushed by compressed air to prolong the service life of the filter element and reduce the The cost of manual filter replacement.
- a supplementary cooling fan is reduced through the unique air flow channel structure design of the heat exchanger.
- the heat exchanger can store the residual heat after heating for heating of fresh air. The utilization rate of waste heat is improved, and the energy consumption of the system is reduced.
- the high-temperature gas after catalytic oxidation is used in the desorption system to cyclically purge the adsorption unit.
- the purified high-temperature gas is exchanged with outdoor fresh air through a heat exchanger. After heat exchange, the original gas is discharged to the outside, and the heated fresh air is used to thermally purge the adsorption unit, which effectively avoids the deposition of organic waste gas in the pipeline and improves the stability and safety of desorption.
- the modular structure design is adopted. The installation and pre-commissioning of all modules and components are completed in the factory. After sending to the site, only the corresponding modules need to be connected, which greatly reduces the workload of the site, and also solves the problem. The deviation caused by production or installation ensures the overall airtightness of the equipment, and the overall appearance is beautiful.
- Fig. 1 is the overall schematic diagram of the present invention
- Fig. 2 is the overall front view of the present invention
- Fig. 3 is the overall plan view of the present invention.
- Fig. 4 is the overall left side view of the present invention.
- Fig. 5 is the internal structure schematic diagram of the present invention.
- Fig. 6 is the schematic diagram of the heat exchanger of the present invention.
- 1-Pretreatment module 2-Adsorption concentration module, 3-Power and catalytic combustion module.
- 101- Access door of pretreatment module 102- Differential pressure display instrument, 103- Air inlet, 104- Hoisting plate, 105- Water retaining groove, 106- Baffle plate, 107- Duster, 108- Filter cartridge, 109- Ash Barrel, 110 - Backflush device.
- 201-Adsorption material installation door 202-Top access door, 203-Adsorption air inlet valve, 204-Adsorption layer, 205-Desorption pipeline.
- the combined modular high-efficiency exhaust gas purification integrated machine is provided with a hoisting plate 104 and a water retaining groove 105 on the top.
- the hoisting plate is used for hoisting, and the water retaining groove is used for water blocking and waterproofing.
- It mainly includes a pretreatment module 1, an adsorption concentration module 2 and a power and catalytic combustion module 3.
- Each module is a work unit with independent functions, including a base, a shell and a module body fixed on the base; the modules are connected in series or in parallel, and bolts, flanges, etc. can be used to tighten the modules.
- Firmware or on-site welding are used for connection, and the module connection is tightly sealed and easy to disassemble.
- the pretreatment module is used for the purification and collection of paint mist particles in the exhaust gas, and mainly includes a guide chamber, a powder spraying chamber and a filter chamber.
- the side wall of the guide chamber is provided with an air inlet 103, and the air inlet is used for Input of organic waste gas containing paint mist particles.
- the rear end of the air inlet is provided with a baffle plate 106, the baffle plate has a certain retention angle and plate spacing, and is used for inducing the airflow direction and reducing the wind speed, so as to avoid the rapid airflow directly impacting the filter material.
- the top of the powder spraying chamber is provided with a powder sprayer 107, which can spray talc powder into the exhaust gas to mix with it, and the talc powder adheres to the surface of the viscous paint mist to eliminate the viscosity of the paint mist.
- a filter cartridge 108 is installed horizontally or vertically in the filter chamber.
- the filter cartridge has a circular or elliptical structure with a rigid support inside, and the surface is made of wood pulp fiber paper or polyester non-woven fabric.
- the filter cartridge can finely filter the paint mist particles in the exhaust gas, so that the concentration of the particles entering the subsequent modules is less than or equal to 1 mg/m 3 .
- the bottom of the filter cartridge is provided with an ash bucket 109, and the ash bucket is connected to the ash bucket in the form of cylinder lifting.
- a backflushing device 110 is installed in the filter chamber, and the paint mist particles attached to the surface of the filter material can be pulsed backflushed by the backflushing action of compressed air.
- the cleaning process is automatically controlled by the pulse controller. Particles fall into the bottom ash bucket.
- Pressure sensors are installed at both ends of the filter cartridge to monitor the change of the pressure difference at both ends of the filter cartridge in real time, and automatic backflushing is performed when the pressure at both ends exceeds a limit value.
- the preprocessing module is also equipped with a differential pressure display instrument 102 .
- the installation position of the filter cartridge is provided with a pretreatment module inspection door 101 to facilitate the inspection and replacement of the filter element.
- the adsorption and concentration module 2 is used for the adsorption and concentration of volatile organic compounds in the exhaust gas.
- the air inlet end of the adsorption and concentration module is provided with an adsorption air inlet valve 203.
- the adsorption and concentration module is equipped with an adsorption material installation door 201 and a top inspection door 202.
- a plurality of independent adsorption units are arranged in the module, and the adsorption units are composed of an adsorption layer 204.
- the adsorption layer includes an adsorption box body and a solid porous adsorption material filled in the adsorption box body.
- the shell of the adsorption and concentration module is drawn and matched, and the bottom of the adsorption box is a mesh plate; the adsorption material is activated carbon or molecular sieve with honeycomb structure.
- the power and catalytic combustion module 3 is used to provide power to pump the exhaust gas from the generation source into the integrated equipment through the pipeline, and to purge the adsorption layer 204 with hot air to regenerate and analyze the adsorbent material.
- the concentrated exhaust gas enters the catalytic combustion device 311 and is oxidized into carbon dioxide and water by the action of the catalyst.
- the purified gas will take out a part of the heat and enter the heat exchanger 310 for heat exchange with the outdoor fresh air.
- the desorption fan 312 discharges up to the standard, and after the outdoor fresh air is heated by the heat exchanger, the adsorption unit is purged again.
- the air end is communicated with the air outlet end of the adsorption and concentration module through the air inlet duct 306, and the air outlet end of the adsorption fan is communicated with the air outlet through the air exhaust duct 307, and the air inlet duct is provided with an adsorption air outlet valve 305;
- the heat exchanger is provided with the heat exchanger cold air inlet 3101, the heat exchanger hot air outlet 3102, the heat exchanger hot air inlet 3103 and the heat exchanger cold air outlet 3104, the heat exchanger cold air inlet and the heat exchanger hot air outlet
- the hot air inlet of the heat exchanger is communicated with the cold air outlet of the heat exchanger;
- the air inlet and air outlet of the catalytic combustion device are provided with flame arresters;
- the adsorption concentration module, adsorption fan, heat exchanger, catalytic combustion device The integrated unit of adsorption, desorption and catalytic combustion is formed between it and the desorption fan through the matching desorption pipeline 205, de
- the heat exchanger is provided with several partitions inside, so that a staggered distribution structure of air flow is formed in the inside of the heat exchanger.
- a thermal insulation layer is arranged around the power and catalytic combustion module.
- the adsorption fan and the desorption fan are centrifugal fans.
- the desorption fan adopts an explosion-proof fan.
- the fresh air damper is provided with a fresh air filter.
- All desorption pipes are square or round pipes.
- All pipes are connected by flanges, and the connection is made of high temperature oil-impregnated asbestos packing.
- the industrial coating exhaust gas enters the pretreatment module through the air inlet 103 under the negative pressure of the adsorption fan 308, and the baffle plate at the air inlet induces the airflow to diffuse around, thereby reducing the filtering wind speed.
- the exhaust gas enters the powder spraying chamber, the powder sprayer 107 is turned on, and the talc powder is sprayed into the powder spraying chamber to mix with the viscous paint mist particles.
- the exhaust gas containing paint mist is filtered by the filter cartridge, and the paint mist particles after desticking are attached to the surface of the filter cartridge, and the organic exhaust gas passes through the filter cartridge and enters the next module.
- Both ends of the filter cartridge 108 are equipped with pressure sensors, which can monitor the pressure difference between the two ends of the filter cartridge in real time and display it on the differential pressure display instrument 102 in real time.
- the backflushing device automatically turns on the backflushing, and sprays 0.4-0.6MPa compressed air to the filter cartridge, and the paint mist particles attached to the surface of the filter cartridge fall off under the backflushing of the compressed air. Put it in the ash bucket, and then collect it by the workers and transport it to the professional factory for unified treatment.
- the organic waste gas filtered by the filter cartridge 108 enters the adsorption and concentration module 2, under the adsorption of the adsorption layer, the organic waste gas is adsorbed in the adsorption layer of the porous structure.
- the adsorption material can be either activated carbon, molecular sieve or A new type of adsorbent material.
- the clean air purified by the adsorption layer passes through the adsorption outlet valve, the air inlet duct and the adsorption fan successively, and then is discharged through the exhaust duct and air outlet up to the standard.
- the adsorption fan and the adsorption outlet valve are closed at this time, and the catalytic combustion device starts to preheat.
- the fresh air enters the catalytic combustion device through the fresh air damper and starts to heat. From the cold air outlet of the heat exchanger to the corresponding desorption fan, it is discharged into the atmosphere.
- the corresponding fresh air damper When the heat exchanger is heated to a certain temperature, the corresponding fresh air damper is closed and the corresponding desorption damper is opened. At this time, the outdoor fresh air enters from the cold air inlet of the heat exchanger under the action of the corresponding desorption fan, and is heated by the heat exchanger. The heated fresh air is discharged from the hot air outlet of the heat exchanger and enters the adsorption through the corresponding desorption pipeline. In the concentration module, the heated air purifies the surface of the adsorption layer, analyzes and regenerates the adsorption unit, and the high-concentration organic waste gas is swept out and enters the catalytic combustion device through the corresponding desorption pipeline.
- the treated high-temperature exhaust gas returns to the heat exchanger from the hot air inlet of the heat exchanger, exchanges heat with the outdoor fresh air, releases the heat from the cold air outlet of the heat exchanger, and discharges up to the standard after passing through the corresponding desorption fan. .
- a temperature detector is installed at the air inlet of the adsorption layer, and the temperature detector is used to detect the inlet air temperature; a temperature detector is installed in the catalytic combustion device to detect the catalytic combustion temperature; It is used to detect the temperature of the exhaust gas; a VOCs concentration detector is installed at the air outlet of the desorption fan to detect the VOCs emission concentration.
- the paint mist particles in the exhaust gas are finely filtered by the filter cartridge, and the concentration of particles entering the subsequent modules is less than or equal to 1 mg/m 3 , which can ensure the safe and stable operation of adsorption .
- the paint mist is removed by powder spraying, and it is blown off by pulse backflushing, which prolongs the service life of the filter element and reduces the cost of manual replacement of the filter element.
- the adsorption layer is thermally purged with heated fresh air, which avoids the safety risk caused by the deposition of organic waste gas in the pipeline.
- the waste heat is stored and used for heating of fresh air, which improves the utilization rate of waste heat and reduces the energy consumption of the system.
Abstract
A combined modular integrated machine for efficient purification of exhaust gas, comprising a pre-treatment module (1), an adsorption and concentration module (2) and a power and catalytic combustion module (3); the pre-treatment module (1) comprises a flow guide chamber, a powder booth and a filter chamber, wherein an air inlet (103) is arranged on a side wall of the flow guide chamber, a baffle plate (106) is arranged at the rear end of the air inlet (103), a powder blower (107) is arranged at the top of the powder booth, and a filter cartridge (108) is arranged in the filter chamber; the adsorption and concentration module (2) is internally provided with an adsorption layer (204); and the power and catalytic combustion module (3) comprises an adsorption fan (308), a heat exchanger (310), a catalytic combustion device (311) and a desorption fan (312). The combined modular integrated machine for efficient purification of exhaust gas has the advantages of compact and simple structure, high purification efficiency, stable desorption, high utilization of waste heat, etc., and can effectively remove dust particles and volatile organics in the exhaust gas.
Description
本发明涉及废气治理设备技术领域,具体涉及一种组合式模块化高效废气净化一体机。The invention relates to the technical field of exhaust gas treatment equipment, in particular to a combined modularized high-efficiency exhaust gas purification integrated machine.
自NO
x、SO
x之后,VOCs(挥发性有机物)已经成为影响国民经济、民生安全的新焦点,其不仅具有危害生态系统的特性,还能够作为“催化剂”促进雾霾的产生。由于目前涂装行业存在大量使用有机溶剂,并且生态环境密封条件差,其产生的漆雾及VOCs具有致畸、致癌、致突变作用,对人体和生态系统造成诸多危害。
Since NOx and SOx , VOCs (volatile organic compounds) have become a new focus affecting the national economy and people's livelihood security. They not only have the characteristics of harming the ecosystem, but also can act as a "catalyst" to promote the generation of haze. Due to the large use of organic solvents in the coating industry and the poor sealing conditions of the ecological environment, the paint mist and VOCs produced by them have teratogenic, carcinogenic and mutagenic effects, causing many harm to the human body and the ecosystem.
目前,对于涂装行业中的废气治理,一部分采用“活性炭吸附”、“光催化”、“低温等离子”等单一治理工艺,这种单一治理工艺普遍存在净化效率低、吸附容量有限,活性炭更换频繁、排放废气浓度波动大等问题。另一部分采用“活性炭吸附、脱附+催化燃烧”的组合式工艺,这类型组合工艺对废气净化的效果普遍比单一治理工艺效果好,但也存在以下问题:(1)前端颗粒物过滤不干净,影响吸附剂的吸附效率,且滤材更换频繁,人工成本高;(2)余热利用率低,能耗大;(3)由于催化燃烧装置不能将有机废气完全净化,未净化完全的有机废气持续在脱附系统内进行循环吹扫,不仅脱附效率低,还存在安全风险;(4)所有风机、管道、阀门均在现场组装,现场管路复杂,泄露率高,且设备占地面积大。At present, for exhaust gas treatment in the coating industry, some single treatment processes such as "activated carbon adsorption", "photocatalysis", and "low temperature plasma" are used. This single treatment process generally has low purification efficiency, limited adsorption capacity, and frequent replacement of activated carbon. , The concentration of exhaust gas fluctuates greatly. The other part adopts the combined process of "activated carbon adsorption, desorption + catalytic combustion". The effect of this type of combined process on exhaust gas purification is generally better than that of a single treatment process, but there are also the following problems: (1) The front-end particulate matter is not filtered cleanly, It affects the adsorption efficiency of the adsorbent, and the filter material is replaced frequently, and the labor cost is high; (2) the utilization rate of waste heat is low, and the energy consumption is large; (3) because the catalytic combustion device cannot completely purify the organic waste gas, the unpurified organic waste gas continues to Cyclic purging in the desorption system not only has low desorption efficiency, but also has safety risks; (4) All fans, pipes, and valves are assembled on-site. The on-site pipeline is complex, the leakage rate is high, and the equipment occupies a large area. .
有鉴于此,本发明解决的技术问题:针对现有活性炭吸附、脱附+催化燃烧工艺前端颗粒物过滤不净、更换滤材难、余热利用率低、脱附不稳定、现场管路复杂、占地面积大等问题,提供一种组合式模块化高效废气净化一体机,使其具有结构紧凑简单、净化效率高、脱附稳定、余热利用率高等优点,可以有效去除废气中的粉尘颗粒物及挥发性有机物。In view of this, the technical problems solved by the present invention are as follows: for the existing activated carbon adsorption, desorption + catalytic combustion process, the front-end particulate matter is not filtered cleanly, it is difficult to replace the filter material, the utilization rate of waste heat is low, the desorption is unstable, the on-site pipeline is complex, and the To solve the problems of large floor area and other problems, a combined modular and efficient exhaust gas purification integrated machine is provided, which has the advantages of compact and simple structure, high purification efficiency, stable desorption and high utilization rate of waste heat, and can effectively remove dust particles and volatilization in the exhaust gas. Sexual organic matter.
本发明通过以下技术手段解决上述问题:The present invention solves the above-mentioned problems through the following technical means:
一种组合式模块化高效废气净化一体机,包括预处理模块、吸附浓缩模块和动力及催化燃烧模块;所述预处理模块包括导流室、喷粉室和过滤室,所述导流室的侧壁设置有进风口,所述进风口的后端设有折流板,所述喷粉室的顶部设置有喷粉器,所述过滤室内安装有滤筒,所述滤筒的底部设置有灰桶;所述吸附浓缩模块内设置有吸附层;所述动力及催化燃烧模块包括吸附风机、换热器、催化燃烧装置和脱附风机,所述吸附浓缩模块、吸附风机、换热器、催化燃烧装置和脱附风机之间通过配套的脱附管道、脱附风阀、新风管道和新风风阀构成吸附脱附及催化燃烧一体单元。A combined modularized high-efficiency exhaust gas purification integrated machine includes a pretreatment module, an adsorption concentration module, and a power and catalytic combustion module; the pretreatment module includes a guide chamber, a powder spraying chamber, and a filter chamber, and the guide chamber has a The side wall is provided with an air inlet, the rear end of the air inlet is provided with a baffle, the top of the dusting chamber is provided with a duster, the filter chamber is provided with a filter cartridge, and the bottom of the filter cartridge is provided with a an ash bucket; an adsorption layer is arranged in the adsorption concentration module; the power and catalytic combustion module includes an adsorption fan, a heat exchanger, a catalytic combustion device and a desorption fan, and the adsorption concentration module, the adsorption fan, the heat exchanger, Between the catalytic combustion device and the desorption fan, an integrated unit of adsorption, desorption and catalytic combustion is formed through the matching desorption pipeline, desorption damper, fresh air pipeline and fresh air damper.
进一步,所述过滤室安装有反吹装置。Further, the filter chamber is provided with a backflushing device.
进一步,所述滤筒的两端设置有压力传感器,滤筒的安装位置设置有预处理模块检修门,预处理模块还配备有压差显示仪表。Further, the two ends of the filter cartridge are provided with pressure sensors, the installation position of the filter cartridge is provided with a pretreatment module inspection door, and the pretreatment module is also equipped with a differential pressure display instrument.
进一步,所述吸附层包括吸附盒体和填充在吸附盒体内的固态多孔状吸附材料,所述吸附盒体通过导轨与吸附浓缩模块的壳体抽拉配合,吸附盒体的底部为网板;所述吸附材料为蜂窝状结构的活性炭或分子筛。Further, the adsorption layer includes an adsorption box body and a solid porous adsorption material filled in the adsorption box body, the adsorption box body is drawn and matched with the shell of the adsorption concentration module through the guide rail, and the bottom of the adsorption box body is a mesh plate; The adsorbent material is activated carbon or molecular sieve with honeycomb structure.
进一步,所述吸附浓缩模块配备有吸附材料安装门和顶部检修门。Further, the adsorption concentration module is equipped with an adsorption material installation door and a top access door.
进一步,所述动力及催化燃烧模块配备有新风百叶窗、排风口和动力及催化燃烧模块检修门。Further, the power and catalytic combustion modules are equipped with fresh air shutters, air outlets and access doors for the power and catalytic combustion modules.
进一步,所述吸附风机的进风端通过进风管道与吸附浓缩模块的出风端连通,吸附风机的出风端通过排风管道与排风口连通,所述进风管道上设置有吸附出风阀。Further, the air inlet end of the adsorption fan is communicated with the air outlet end of the adsorption concentration module through the air inlet duct, and the air outlet end of the adsorption fan is communicated with the air outlet through the air outlet duct, and the air inlet duct is provided with an adsorption outlet. damper.
进一步,所述换热器设置有换热器冷风进风口、换热器热风出风口、换热器热风进风口和换热器冷风出风口,换热器冷风进风口与换热器热风出风口连通,换热器热风进风口与换热器冷风出风口连通。Further, the heat exchanger is provided with the heat exchanger cold air inlet, the heat exchanger hot air outlet, the heat exchanger hot air inlet and the heat exchanger cold air outlet, the heat exchanger cold air inlet and the heat exchanger hot air outlet. The hot air inlet of the heat exchanger is communicated with the cold air outlet of the heat exchanger.
进一步,所述催化燃烧装置的进风口及出风口均设置有阻火器。Further, both the air inlet and the air outlet of the catalytic combustion device are provided with flame arresters.
进一步,吸附层的进风端、催化燃烧装置内部和换热器冷风出风口均设置有温度检测,所述脱附风机出风口处设置有VOCs浓度检测。Further, the air inlet end of the adsorption layer, the interior of the catalytic combustion device and the cold air outlet of the heat exchanger are all provided with temperature detection, and the air outlet of the desorption fan is provided with VOCs concentration detection.
1、对废气中的粘性漆雾颗粒进行消粘并精细过滤,过滤后的颗粒物浓度≤1mg/m
3,并且通过压缩空气对滤筒的滤芯进行自动脉冲反吹,延长滤芯使用寿命,减少了人工更换滤芯的成本。
1. Detackify and finely filter the viscous paint mist particles in the exhaust gas. The concentration of the filtered particles is less than or equal to 1mg/m 3 , and the filter element of the filter cartridge is automatically pulsed backflushed by compressed air to prolong the service life of the filter element and reduce the The cost of manual filter replacement.
2、通过换热器独特气流孔道的结构设计,相比于原有活性炭吸附脱附系统减少了一台补冷风机,同时换热器可将加热后的余热存留下来,用于新风的加热,提高了余热利用率,降低了系统能耗。2. Compared with the original activated carbon adsorption and desorption system, a supplementary cooling fan is reduced through the unique air flow channel structure design of the heat exchanger. At the same time, the heat exchanger can store the residual heat after heating for heating of fresh air. The utilization rate of waste heat is improved, and the energy consumption of the system is reduced.
3、相比于原有活性炭吸附脱附系统中采用催化氧化后的高温气体在脱附系统内对吸附单元进行循环吹扫,本发明通过换热器将净化后的高温气体与室外新风进行换热,换热后原有气体排出室外,同时加热后的新风对吸附单元进行热吹扫,有效避免管道内有机废气的沉积,提高了脱附的稳定性和安全性。3. Compared with the original activated carbon adsorption and desorption system, the high-temperature gas after catalytic oxidation is used in the desorption system to cyclically purge the adsorption unit. In the present invention, the purified high-temperature gas is exchanged with outdoor fresh air through a heat exchanger. After heat exchange, the original gas is discharged to the outside, and the heated fresh air is used to thermally purge the adsorption unit, which effectively avoids the deposition of organic waste gas in the pipeline and improves the stability and safety of desorption.
4、采用模块化结构设计,所有模块及部件的安装及预调试均在工厂内完成,发往现场后只需要连接相应的模块即可,极大的减少了现场的工作量,同时还解决了因制作或安装造成的偏差,保证了设备整体的气密性,且整体美观大气。4. The modular structure design is adopted. The installation and pre-commissioning of all modules and components are completed in the factory. After sending to the site, only the corresponding modules need to be connected, which greatly reduces the workload of the site, and also solves the problem. The deviation caused by production or installation ensures the overall airtightness of the equipment, and the overall appearance is beautiful.
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据提供的附图获得其他的附图。In order to explain the embodiments of the present invention or the technical solutions in the prior art more clearly, the following briefly introduces the accompanying drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only It is an embodiment of the present invention. For those of ordinary skill in the art, other drawings can also be obtained according to the provided drawings without creative work.
图1为本发明的整体示意图;Fig. 1 is the overall schematic diagram of the present invention;
图2为本发明的整体主视图;Fig. 2 is the overall front view of the present invention;
图3为本发明的整体俯视图;Fig. 3 is the overall plan view of the present invention;
图4为本发明的整体左视图;Fig. 4 is the overall left side view of the present invention;
图5为本发明的内部结构示意图;Fig. 5 is the internal structure schematic diagram of the present invention;
图6为本发明的换热器示意图;Fig. 6 is the schematic diagram of the heat exchanger of the present invention;
图中标号:Labels in the figure:
1-预处理模块,2-吸附浓缩模块,3-动力及催化燃烧模块。1-Pretreatment module, 2-Adsorption concentration module, 3-Power and catalytic combustion module.
101-预处理模块检修门,102-压差显示仪表,103-进风口,104-吊装板,105-挡水槽,106-折流板,107-喷粉器,108-滤筒,109-灰桶,110-反吹装置。101- Access door of pretreatment module, 102- Differential pressure display instrument, 103- Air inlet, 104- Hoisting plate, 105- Water retaining groove, 106- Baffle plate, 107- Duster, 108- Filter cartridge, 109- Ash Barrel, 110 - Backflush device.
201-吸附材料安装门,202-顶部检修门,203-吸附进风阀,204-吸附层,205-脱附管道。201-Adsorption material installation door, 202-Top access door, 203-Adsorption air inlet valve, 204-Adsorption layer, 205-Desorption pipeline.
301-新风百叶窗,302-排风口,303-动力及催化燃烧模块检修门,304-脱附阀门,305-吸附出风阀,306-进风管道,307-排风管道,308-吸附风机,309-新风风阀,310-换热器,311-催化燃烧装置,312-脱附风机。301- Fresh air shutter, 302- Air outlet, 303- Power and catalytic combustion module access door, 304- Desorption valve, 305- Adsorption air valve, 306- Air inlet duct, 307- Exhaust duct, 308- Adsorption fan , 309- fresh air valve, 310- heat exchanger, 311- catalytic combustion device, 312- desorption fan.
3101-换热器冷风进风口,3102-换热器热风出风口,3103-换热器热风进风口,3104换热器冷风出风口。3101- heat exchanger cold air inlet, 3102- heat exchanger hot air outlet, 3103- heat exchanger hot air inlet, 3104 heat exchanger cold air outlet.
为了使本技术领域的人员更好地理解本申请中的技术方案,下面将结合本申请实施例中的附图,对本申请实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本申请一部分实施例,而不是全部的实施例。基于本申请中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都应当属于本申请保护的范围。In order to make those skilled in the art better understand the technical solutions in the present application, the technical solutions in the embodiments of the present application will be described clearly and completely below with reference to the accompanying drawings in the embodiments of the present application. Obviously, the described The embodiments are only a part of the embodiments of the present application, but not all of the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without creative work shall fall within the scope of protection of the present application.
在本发明的描述中,需要理解的是,术语“前”、“后”、“左”、“右”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 orientations or positional relationships indicated by the terms "front", "rear", "left", "right", etc. are based on the orientations or positional relationships shown in the accompanying drawings, only for the purpose of It is convenient to describe the present invention and to simplify the description, rather than indicating or implying that the device or element referred to must have a particular orientation, be constructed and operate in a particular orientation, and therefore should not be construed as limiting the invention.
如图1至图6所示,本发明提供的组合式模块化高效废气净化一体机,其顶部设置有吊装板104和挡水槽105,吊装板用于吊装,挡水槽用于挡水、防水。主要包括预处理模块1、吸附浓缩模块2和动力及催化燃烧模块3。每个模块为具有独立功能的工作单元,均包括底座、壳体和固定在底座上的模块主体;模块与模块之间采用串联或并联的形式,模块与模块之间可用螺栓、法兰等紧固件或者现场焊接进行连接,并且模块连接处密封紧密,且拆装方便。As shown in FIGS. 1 to 6 , the combined modular high-efficiency exhaust gas purification integrated machine provided by the present invention is provided with a hoisting plate 104 and a water retaining groove 105 on the top. The hoisting plate is used for hoisting, and the water retaining groove is used for water blocking and waterproofing. It mainly includes a pretreatment module 1, an adsorption concentration module 2 and a power and catalytic combustion module 3. Each module is a work unit with independent functions, including a base, a shell and a module body fixed on the base; the modules are connected in series or in parallel, and bolts, flanges, etc. can be used to tighten the modules. Firmware or on-site welding are used for connection, and the module connection is tightly sealed and easy to disassemble.
所述预处理模块用于废气中漆雾颗粒的净化与收集,主要包括导流室、喷粉室和过滤室,所述导流室的侧壁设置有进风口103,所述进风口用于含有漆雾颗粒的有机废气输入。进风口的后端设有折流板106,所述折流板具有一定的折留角度及板间距,用于诱导气流走向及降低风速的作用,以避免快速的气流直接冲击滤材。所述喷粉室的顶部设置有喷粉器107,可向废气中喷入滑石粉与之混合,滑石粉附着在粘性漆雾表面上,消除漆雾粘性。所述过滤室内水平或竖直安装有滤筒108,滤筒的滤芯采用圆形或者椭圆形结构,内部具有刚性支撑,表面为木浆纤维纸或聚酯无纺布。滤筒可对废气中的漆雾颗粒进行精细过滤,使进入到后续模块的颗粒物浓度≤1mg/m
3。所述滤筒的底部设置有灰桶109,所述灰桶采用气缸提升的形式与灰斗进行连接。
The pretreatment module is used for the purification and collection of paint mist particles in the exhaust gas, and mainly includes a guide chamber, a powder spraying chamber and a filter chamber. The side wall of the guide chamber is provided with an air inlet 103, and the air inlet is used for Input of organic waste gas containing paint mist particles. The rear end of the air inlet is provided with a baffle plate 106, the baffle plate has a certain retention angle and plate spacing, and is used for inducing the airflow direction and reducing the wind speed, so as to avoid the rapid airflow directly impacting the filter material. The top of the powder spraying chamber is provided with a powder sprayer 107, which can spray talc powder into the exhaust gas to mix with it, and the talc powder adheres to the surface of the viscous paint mist to eliminate the viscosity of the paint mist. A filter cartridge 108 is installed horizontally or vertically in the filter chamber. The filter cartridge has a circular or elliptical structure with a rigid support inside, and the surface is made of wood pulp fiber paper or polyester non-woven fabric. The filter cartridge can finely filter the paint mist particles in the exhaust gas, so that the concentration of the particles entering the subsequent modules is less than or equal to 1 mg/m 3 . The bottom of the filter cartridge is provided with an ash bucket 109, and the ash bucket is connected to the ash bucket in the form of cylinder lifting.
所述过滤室内安装有反吹装置110,通过压缩空气的反吹作用可将附着在滤材表面的漆雾颗粒进行脉冲反吹,清灰过程由脉冲控制仪自动控制,反吹后的漆雾颗粒落入底部灰桶中。A backflushing device 110 is installed in the filter chamber, and the paint mist particles attached to the surface of the filter material can be pulsed backflushed by the backflushing action of compressed air. The cleaning process is automatically controlled by the pulse controller. Particles fall into the bottom ash bucket.
所述滤筒的两端安装有压力传感器,对滤筒两端的压差变化实时监控,当两端压力超过限定值后实施自动反吹。预处理模块还配备有压差显示仪表102。Pressure sensors are installed at both ends of the filter cartridge to monitor the change of the pressure difference at both ends of the filter cartridge in real time, and automatic backflushing is performed when the pressure at both ends exceeds a limit value. The preprocessing module is also equipped with a differential pressure display instrument 102 .
所述滤筒的安装位置设置有预处理模块检修门101,以方便对滤芯进行检修与更换。The installation position of the filter cartridge is provided with a pretreatment module inspection door 101 to facilitate the inspection and replacement of the filter element.
所述吸附浓缩模块2用于废气中挥发性有机物的吸附浓缩,吸附浓缩模块的进风端设置有吸附进风阀203,吸附浓缩模块配备有吸附材料安装门201和顶部检修门202,吸附浓缩模块内设置有多个独立的吸附单元,所述吸附单元由吸附层204构成,所述吸附层包括吸附盒体和填充在吸附盒体内的固态多孔状吸附材料,所述吸附盒体通过导轨与吸附浓缩模块的壳体抽拉配合,吸附盒体的底部为网板;所述吸附材料为蜂窝状结构的活性炭或分子筛。The adsorption and concentration module 2 is used for the adsorption and concentration of volatile organic compounds in the exhaust gas. The air inlet end of the adsorption and concentration module is provided with an adsorption air inlet valve 203. The adsorption and concentration module is equipped with an adsorption material installation door 201 and a top inspection door 202. A plurality of independent adsorption units are arranged in the module, and the adsorption units are composed of an adsorption layer 204. The adsorption layer includes an adsorption box body and a solid porous adsorption material filled in the adsorption box body. The shell of the adsorption and concentration module is drawn and matched, and the bottom of the adsorption box is a mesh plate; the adsorption material is activated carbon or molecular sieve with honeycomb structure.
所述动力及催化燃烧模块3用于提供动力将废气从产生源处通过管道抽入一体化设备中,并将吸附层204通过热空气吹扫,对吸附材料进行再生解析,再生解析产生的高浓度废气进入到催化燃烧装置311内,通过催化剂的作用氧化为二氧化碳和水,净化后的气体会带出一部分热量,进入到换热器310中与室外新风进行热交换,将其热量释放后通过脱附风机312达标排放,而室外新风在经过换热器加热后,重新对吸附单元进行吹扫。其配备有新风百叶窗301、排风口302和动力及催化燃烧模块检修门303,主要包括:吸附风机308、换热器310、催化燃烧装置311和脱附风机312,所述吸附风机308的进风端通过进风管道306与吸附浓缩模块的出风端连通,吸附风机的出风端通过排风管道307与排风口连通,所述进风管道上设置有吸附出风阀305;所述换热器设置有换热器冷风进风口3101、换热器热风出风口3102、换热器热风进风口3103和换热器冷风出风口3104,换热器冷风进风口与换热器热风出风口连通,换热器热风进风口与换热器冷风出风口连通;所述催化燃烧装置的进风口及出风口均设置有阻火器;所述吸附浓缩模块、吸附风机、换热器、催化燃烧装置和脱附风机之间通过配套的脱附管道205、脱附风阀304、新风管道和新风风阀309构成吸附脱附及催化燃烧一体单元,具体的管道和阀门布置均为现有技术,这里不做详细说明。The power and catalytic combustion module 3 is used to provide power to pump the exhaust gas from the generation source into the integrated equipment through the pipeline, and to purge the adsorption layer 204 with hot air to regenerate and analyze the adsorbent material. The concentrated exhaust gas enters the catalytic combustion device 311 and is oxidized into carbon dioxide and water by the action of the catalyst. The purified gas will take out a part of the heat and enter the heat exchanger 310 for heat exchange with the outdoor fresh air. The desorption fan 312 discharges up to the standard, and after the outdoor fresh air is heated by the heat exchanger, the adsorption unit is purged again. It is equipped with fresh air shutters 301, an air outlet 302 and a power and catalytic combustion module access door 303, mainly including: an adsorption fan 308, a heat exchanger 310, a catalytic combustion device 311 and a desorption fan 312. The air end is communicated with the air outlet end of the adsorption and concentration module through the air inlet duct 306, and the air outlet end of the adsorption fan is communicated with the air outlet through the air exhaust duct 307, and the air inlet duct is provided with an adsorption air outlet valve 305; The heat exchanger is provided with the heat exchanger cold air inlet 3101, the heat exchanger hot air outlet 3102, the heat exchanger hot air inlet 3103 and the heat exchanger cold air outlet 3104, the heat exchanger cold air inlet and the heat exchanger hot air outlet The hot air inlet of the heat exchanger is communicated with the cold air outlet of the heat exchanger; the air inlet and air outlet of the catalytic combustion device are provided with flame arresters; the adsorption concentration module, adsorption fan, heat exchanger, catalytic combustion device The integrated unit of adsorption, desorption and catalytic combustion is formed between it and the desorption fan through the matching desorption pipeline 205, desorption damper 304, fresh air pipeline and fresh air damper 309. The specific pipeline and valve arrangement are all in the prior art, here Do not go into detail.
所述换热器内部具有若干个隔板,使其内部形成气流交错的孔道分布结构。The heat exchanger is provided with several partitions inside, so that a staggered distribution structure of air flow is formed in the inside of the heat exchanger.
所述动力及催化燃烧模块四周设置有保温层。A thermal insulation layer is arranged around the power and catalytic combustion module.
所述吸附风机和脱附风机采用离心式风机。The adsorption fan and the desorption fan are centrifugal fans.
所述脱附风机采用防爆型风机。The desorption fan adopts an explosion-proof fan.
所述新风风阀设置有新风过滤器。The fresh air damper is provided with a fresh air filter.
所有脱附管道均采用方形或圆形管道。All desorption pipes are square or round pipes.
所有管道均采用法兰形式连接,连接处为耐高温浸油石棉盘根。All pipes are connected by flanges, and the connection is made of high temperature oil-impregnated asbestos packing.
吸附阶段时:工业涂装废气在吸附风机308的负压作用下,通过进风口103进入到预处理模块内,位于进风口处的折流板诱导气流向四周扩散,从而使过滤风速降低。废气进入到喷粉室内,喷粉器107打开,将滑石粉喷入喷粉室内,使其与粘性的漆雾颗粒混合,滑石粉附着在粘性漆雾表面,消除漆雾粘性。之后,含有漆雾的废气经滤筒过滤,其中消粘后的漆雾颗粒附着在滤筒表面,有机废气则通滤筒,进入下一模块。During the adsorption stage: the industrial coating exhaust gas enters the pretreatment module through the air inlet 103 under the negative pressure of the adsorption fan 308, and the baffle plate at the air inlet induces the airflow to diffuse around, thereby reducing the filtering wind speed. The exhaust gas enters the powder spraying chamber, the powder sprayer 107 is turned on, and the talc powder is sprayed into the powder spraying chamber to mix with the viscous paint mist particles. After that, the exhaust gas containing paint mist is filtered by the filter cartridge, and the paint mist particles after desticking are attached to the surface of the filter cartridge, and the organic exhaust gas passes through the filter cartridge and enters the next module.
滤筒108的两端装有压力传感器,可对滤筒两端的压差实时监控并在压差显示仪表102上实时显示。随着滤筒两端的压差逐渐增大,反吹装置自动打开反吹,将0.4-0.6MPa压缩空气喷向滤筒,附着在滤筒表面的漆雾颗粒在压缩空气的反吹下掉落至灰桶中,再由工人收集后运输至专业厂家统一处理。Both ends of the filter cartridge 108 are equipped with pressure sensors, which can monitor the pressure difference between the two ends of the filter cartridge in real time and display it on the differential pressure display instrument 102 in real time. As the pressure difference between the two ends of the filter cartridge gradually increases, the backflushing device automatically turns on the backflushing, and sprays 0.4-0.6MPa compressed air to the filter cartridge, and the paint mist particles attached to the surface of the filter cartridge fall off under the backflushing of the compressed air. Put it in the ash bucket, and then collect it by the workers and transport it to the professional factory for unified treatment.
经滤筒108过滤后的有机废气进入到吸附浓缩模块2后,在吸附层的吸附作用下,有机废气被吸附在多孔结构的吸附层内,该吸附材料既可以是活性炭,也可以是分子筛或某种新型吸附材料。经吸附层净化后的洁净空气先后通过吸附出风阀,进风管道、吸附风机后,经由排风管道、排风口达标排放。After the organic waste gas filtered by the filter cartridge 108 enters the adsorption and concentration module 2, under the adsorption of the adsorption layer, the organic waste gas is adsorbed in the adsorption layer of the porous structure. The adsorption material can be either activated carbon, molecular sieve or A new type of adsorbent material. The clean air purified by the adsorption layer passes through the adsorption outlet valve, the air inlet duct and the adsorption fan successively, and then is discharged through the exhaust duct and air outlet up to the standard.
脱附阶段时:当废气吸附到一定浓度后,此时吸附风机及吸附出风阀关闭,催化燃烧装置开始预热,当加热到一定温度后,对应的脱附风机和新风风阀打开,室外新风在对应的脱附风机负压的作用下,通过新风风阀进入到催化燃烧装置内开始加热,加热后的空气从换热器热风进风口进入,经交错的气流孔道后将热量储存,再从换热器冷风出风口至对应的脱附风机后排入至大气中。In the desorption stage: when the exhaust gas is adsorbed to a certain concentration, the adsorption fan and the adsorption outlet valve are closed at this time, and the catalytic combustion device starts to preheat. Under the action of the negative pressure of the corresponding desorption fan, the fresh air enters the catalytic combustion device through the fresh air damper and starts to heat. From the cold air outlet of the heat exchanger to the corresponding desorption fan, it is discharged into the atmosphere.
当换热器升温到一定温度后,对应的新风风阀关闭,对应的脱附风阀打开。此时室外新风在对应脱附风机的作用下,从换热器冷风进风口进入,经过换热器进行加热,加热后的新风从换热器热风出风口排出,经对应的脱附管道进入吸附浓缩模块,加热后的空气对吸附层表面进行热吹扫,对吸附单元进行解析再生,高浓度的有机废气被吹扫出来,通过对应的脱附管道进入至催化燃烧装置内,在催化剂作用下氧化为二氧化碳和水,同时放出一部分热量。处理后的高温尾气从换热器热风进风口重新回至换热器内,与室外的新风进行热交换,将热量释放后从换热器冷风出风口排出,经对应的脱附风机后达标排放。When the heat exchanger is heated to a certain temperature, the corresponding fresh air damper is closed and the corresponding desorption damper is opened. At this time, the outdoor fresh air enters from the cold air inlet of the heat exchanger under the action of the corresponding desorption fan, and is heated by the heat exchanger. The heated fresh air is discharged from the hot air outlet of the heat exchanger and enters the adsorption through the corresponding desorption pipeline. In the concentration module, the heated air purifies the surface of the adsorption layer, analyzes and regenerates the adsorption unit, and the high-concentration organic waste gas is swept out and enters the catalytic combustion device through the corresponding desorption pipeline. Under the action of the catalyst Oxidized into carbon dioxide and water, while releasing part of the heat. The treated high-temperature exhaust gas returns to the heat exchanger from the hot air inlet of the heat exchanger, exchanges heat with the outdoor fresh air, releases the heat from the cold air outlet of the heat exchanger, and discharges up to the standard after passing through the corresponding desorption fan. .
在吸附层进风口处装有温度检测,温度检测用于检测进风温度;在催化燃烧装置内装有温度检测,用于检测催化燃烧温度;在换热器冷风出风口处装有温度检测,用于检测排放气体温度;在脱附风机出风口处装有VOCs浓度检测,用于检测VOCs排放浓度。A temperature detector is installed at the air inlet of the adsorption layer, and the temperature detector is used to detect the inlet air temperature; a temperature detector is installed in the catalytic combustion device to detect the catalytic combustion temperature; It is used to detect the temperature of the exhaust gas; a VOCs concentration detector is installed at the air outlet of the desorption fan to detect the VOCs emission concentration.
综上所述,采用本发明的废气净化一体机,一方面,废气中的漆雾颗粒经滤筒的精细过滤,进入到后续模块的颗粒物浓度≤1mg/m
3,可保证吸附安全稳定地运行。同时,通过喷粉对漆雾进行消粘,并用脉冲反吹将其吹落,延长了滤芯的使用寿命,减少了人工更换滤芯的成本。另一方面,通过换热器独特气流孔道的结构设计,采用加热的新风对吸附层进行热吹扫,避免了有机废气在管道内的沉积而产生的安全风险,同时换热器可将加热后的余热存留下来,用于新风的加热,提高了余热利用率,降低了系统能耗。
In summary, using the exhaust gas purification integrated machine of the present invention, on the one hand, the paint mist particles in the exhaust gas are finely filtered by the filter cartridge, and the concentration of particles entering the subsequent modules is less than or equal to 1 mg/m 3 , which can ensure the safe and stable operation of adsorption . At the same time, the paint mist is removed by powder spraying, and it is blown off by pulse backflushing, which prolongs the service life of the filter element and reduces the cost of manual replacement of the filter element. On the other hand, through the structural design of the unique airflow channel of the heat exchanger, the adsorption layer is thermally purged with heated fresh air, which avoids the safety risk caused by the deposition of organic waste gas in the pipeline. The waste heat is stored and used for heating of fresh air, which improves the utilization rate of waste heat and reduces the energy consumption of the system.
最后说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的宗旨和范围,其均应涵盖在本发明的权利要求范围当中。Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be Modifications or equivalent substitutions without departing from the spirit and scope of the technical solutions of the present invention should be included in the scope of the claims of the present invention.
Claims (10)
- 一种组合式模块化高效废气净化一体机,其特征在于:包括预处理模块(1)、吸附浓缩模块(2)和动力及催化燃烧模块(3);所述预处理模块包括导流室、喷粉室和过滤室,所述导流室的侧壁设置有进风口(103),所述进风口的后端设有折流板(106),所述喷粉室的顶部设置有喷粉器(107),所述过滤室内安装有滤筒(108),所述滤筒的底部设置有灰桶(109);所述吸附浓缩模块内设置有吸附层(204);所述动力及催化燃烧模块包括吸附风机(308)、换热器(310)、催化燃烧装置(311)和脱附风机(312),所述吸附浓缩模块(2)、吸附风机(308)、换热器(310)、催化燃烧装置(311)和脱附风机(312)之间通过配套的脱附管道(205)、脱附风阀(304)、新风管道和新风风阀(309)构成吸附脱附及催化燃烧一体单元。A combined modularized high-efficiency exhaust gas purification integrated machine is characterized in that: it includes a pretreatment module (1), an adsorption concentration module (2), and a power and catalytic combustion module (3); the pretreatment module includes a guide chamber, a A powder spraying chamber and a filter chamber, the side wall of the guide chamber is provided with an air inlet (103), the rear end of the air inlet is provided with a baffle (106), and the top of the powder spraying chamber is provided with a powder spray A filter (107), a filter cartridge (108) is installed in the filter chamber, and an ash bucket (109) is arranged at the bottom of the filter cartridge; an adsorption layer (204) is arranged in the adsorption and concentration module; the power and catalysis The combustion module includes an adsorption fan (308), a heat exchanger (310), a catalytic combustion device (311) and a desorption fan (312). The adsorption and concentration module (2), the adsorption fan (308), the heat exchanger (310) ), the catalytic combustion device (311) and the desorption fan (312) through the matching desorption pipeline (205), the desorption damper (304), the fresh air pipeline and the fresh air damper (309) to form adsorption and desorption and catalytic Combustion integrated unit.
- 根据权利要求1所述的组合式模块化高效废气净化一体机,其特征在于:所述过滤室安装有反吹装置(110)。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 1, characterized in that: the filter chamber is provided with a backflushing device (110).
- 根据权利要求2所述的组合式模块化高效废气净化一体机,其特征在于:所述滤筒(108)的两端设置有压力传感器,滤筒的安装位置设置有预处理模块检修门(101),预处理模块还配备有压差显示仪表(102)。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 2, characterized in that: the two ends of the filter cartridge (108) are provided with pressure sensors, and the installation position of the filter cartridge is provided with a pretreatment module inspection door (101). ), the preprocessing module is also equipped with a differential pressure display instrument (102).
- 根据权利要求3所述的组合式模块化高效废气净化一体机,其特征在于:所述吸附层(204)包括吸附盒体和填充在吸附盒体内的固态多孔状吸附材料,所述吸附盒体通过导轨与吸附浓缩模块的壳体抽拉配合,吸附盒体的底部为网板;所述吸附材料为蜂窝状结构的活性炭或分子筛。The combined modular high-efficiency exhaust gas purification integrated machine according to claim 3, characterized in that: the adsorption layer (204) comprises an adsorption box body and a solid porous adsorption material filled in the adsorption box body, and the adsorption box body The guide rail is drawn and matched with the shell of the adsorption and concentration module, and the bottom of the adsorption box is a mesh plate; the adsorption material is activated carbon or molecular sieve with honeycomb structure.
- 根据权利要求4所述的组合式模块化高效废气净化一体机,其特征在于:所述吸附浓缩模块配备有吸附材料安装门(201)和顶部检修门(202)。The combined modular high-efficiency exhaust gas purification integrated machine according to claim 4, characterized in that: the adsorption concentration module is equipped with an adsorption material installation door (201) and a top access door (202).
- 根据权利要求5所述的组合式模块化高效废气净化一体机,其特征在于:所述动力及催化燃烧模块配备有新风百叶窗(301)、排风口(302)和动力及催化燃烧模块检修门(303)。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 5, characterized in that: the power and catalytic combustion module is equipped with fresh air shutters (301), an air outlet (302) and a power and catalytic combustion module access door (303).
- 根据权利要求6所述的组合式模块化高效废气净化一体机,其特征在于:所述吸附风机(308)的进风端通过进风管道(306)与吸附浓缩模块的出风端连通,吸附风机的出风端通过排风管道(307)与排风口连通,所述进风管道上设置有吸附出风阀(305)。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 6, characterized in that: the air inlet end of the adsorption fan (308) is communicated with the air outlet end of the adsorption concentration module through the air inlet pipe (306), and the adsorption The air outlet end of the fan is communicated with the air outlet through an air outlet duct (307), and an adsorption air outlet valve (305) is arranged on the air inlet duct.
- 根据权利要求7所述的组合式模块化高效废气净化一体机,其特征在于:所述换热器设置有换热器冷风进风口(3101)、换热器热风出风口(3102)、换热器热风进风口(3103)和换热器冷风出风口(3104),换热器冷风进风口与换热器热风出风口连通,换热器热风进风口与换热器冷风出风口连通。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 7, characterized in that: the heat exchanger is provided with a heat exchanger cold air inlet (3101), a heat exchanger hot air outlet (3102), a heat exchanger The hot air inlet of the heat exchanger (3103) and the cold air outlet of the heat exchanger (3104) are connected.
- 根据权利要求8所述的组合式模块化高效废气净化一体机,其特征在于:所述催化燃烧装置(311)的进风口及出风口均设置有阻火器。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 8, characterized in that: the air inlet and the air outlet of the catalytic combustion device (311) are provided with flame arresters.
- 根据权利要求9所述的组合式模块化高效废气净化一体机,其特征在于:吸附层的进风端、催化燃烧装置内部和换热器冷风出风口均设置有温度检测,所述脱附风机出风口处设置有VOCs浓度检测。The combined modularized high-efficiency exhaust gas purification integrated machine according to claim 9, wherein the air inlet end of the adsorption layer, the interior of the catalytic combustion device and the cold air outlet of the heat exchanger are all provided with temperature detection, and the desorption fan VOCs concentration detection is set at the air outlet.
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CN114797365B (en) * | 2022-05-26 | 2023-09-15 | 江苏建筑职业技术学院 | Integrated waste gas treatment device based on photocatalysis |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105371286A (en) * | 2015-11-10 | 2016-03-02 | 重庆科蓝环保实业有限公司 | Preheat type catalytic combustion system for purifying volatile organic waste gas |
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 |
CN208824192U (en) * | 2018-08-02 | 2019-05-07 | 中南大学 | A kind of VOCs exhaust-gas efficient adsorption/desorption catalyzing burning processing system |
CN110898555A (en) * | 2019-12-05 | 2020-03-24 | 航天凯天环保科技股份有限公司 | Waste gas treatment device |
WO2020116020A1 (en) * | 2018-12-06 | 2020-06-11 | エヌ・イーケムキャット株式会社 | Exhaust gas purging device |
CN111545011A (en) * | 2020-05-11 | 2020-08-18 | 浙江浩博环保设备有限公司 | Activated carbon adsorption, desorption and catalytic combustion all-in-one machine and working method thereof |
CN112892137A (en) * | 2021-01-14 | 2021-06-04 | 航天凯天环保科技股份有限公司 | Modular high-efficient exhaust purification all-in-one of modularization |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102614731B (en) * | 2012-04-05 | 2014-03-26 | 泉州市天龙环境工程有限公司 | Purifying device for paint spraying organic waste gas and solvent recovering method thereof |
CN205886514U (en) * | 2016-08-11 | 2017-01-18 | 杭州佳德环保科技有限公司 | Paint spraying waste gas treatment device |
CN109364599A (en) * | 2018-12-20 | 2019-02-22 | 南京鑫之鸿环保科技有限公司 | A kind of paint spray booth's catalysis burning waste gas treatment process |
CN209763108U (en) * | 2019-02-25 | 2019-12-10 | 重庆三峡环保(集团)有限公司 | Device for treating organic waste gas by active carbon adsorption concentration and catalytic combustion |
CN111939719A (en) * | 2020-08-18 | 2020-11-17 | 深圳义信环保产业发展有限公司 | Device and method for treating automobile maintenance spraying waste gas through activated carbon adsorption, desorption and catalytic combustion |
-
2021
- 2021-01-14 CN CN202110047041.6A patent/CN112892137A/en active Pending
- 2021-07-26 WO PCT/CN2021/108327 patent/WO2022151699A1/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105371286A (en) * | 2015-11-10 | 2016-03-02 | 重庆科蓝环保实业有限公司 | Preheat type catalytic combustion system for purifying volatile organic waste gas |
CN208824192U (en) * | 2018-08-02 | 2019-05-07 | 中南大学 | A kind of VOCs exhaust-gas efficient adsorption/desorption catalyzing burning processing system |
WO2020116020A1 (en) * | 2018-12-06 | 2020-06-11 | エヌ・イーケムキャット株式会社 | Exhaust gas purging device |
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 |
CN110898555A (en) * | 2019-12-05 | 2020-03-24 | 航天凯天环保科技股份有限公司 | Waste gas treatment device |
CN111545011A (en) * | 2020-05-11 | 2020-08-18 | 浙江浩博环保设备有限公司 | Activated carbon adsorption, desorption and catalytic combustion all-in-one machine and working method thereof |
CN112892137A (en) * | 2021-01-14 | 2021-06-04 | 航天凯天环保科技股份有限公司 | Modular high-efficient exhaust purification all-in-one of modularization |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115445591A (en) * | 2022-09-30 | 2022-12-09 | 重庆红源活性炭有限公司 | Automatic active carbon desorption device of board formula |
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