CN110624397A - Microbial waste gas purification device - Google Patents
Microbial waste gas purification device Download PDFInfo
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- CN110624397A CN110624397A CN201911034652.6A CN201911034652A CN110624397A CN 110624397 A CN110624397 A CN 110624397A CN 201911034652 A CN201911034652 A CN 201911034652A CN 110624397 A CN110624397 A CN 110624397A
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- 238000000746 purification Methods 0.000 title claims abstract description 39
- 230000000813 microbial effect Effects 0.000 title claims abstract description 28
- 239000002912 waste gas Substances 0.000 title abstract description 34
- 238000005507 spraying Methods 0.000 claims abstract description 24
- 238000001556 precipitation Methods 0.000 claims abstract description 15
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000001179 sorption measurement Methods 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 244000005700 microbiome Species 0.000 claims abstract description 11
- 238000001035 drying Methods 0.000 claims abstract description 7
- 230000001954 sterilising effect Effects 0.000 claims abstract description 7
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 6
- 239000007789 gas Substances 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 8
- 239000011261 inert gas Substances 0.000 claims description 6
- 239000003463 adsorbent Substances 0.000 claims description 3
- 238000005273 aeration Methods 0.000 claims description 3
- 239000002274 desiccant Substances 0.000 claims description 3
- 239000005416 organic matter Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims 2
- 230000008676 import Effects 0.000 claims 1
- 230000004060 metabolic process Effects 0.000 abstract description 5
- 239000000945 filler Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 229910001872 inorganic gas Inorganic materials 0.000 description 2
- 235000015097 nutrients Nutrition 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical class N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000007269 microbial metabolism Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000011045 prefiltration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000008054 signal transmission Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003573 thiols Chemical class 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/95—Specific microorganisms
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a microbial waste gas purification device, which consists of a fan, a multistage filtering system, an air inlet pipe and a microbial purification device, wherein the microbial purification device sequentially comprises the following components in sequence from left to right: a facultative anaerobic precipitation zone, a buffer zone, an aerobic zone, a drying adsorption layer, a sterilization zone and an exhaust pipe; the microbial purification device is characterized in that a liquid storage layer is arranged at the top of the microbial purification device, a spraying system matched with a facultative anaerobic precipitation area and an aerobic area is arranged in the liquid storage layer, and a temperature compensation system matched with the spraying system is arranged on the facultative anaerobic precipitation area and the aerobic area. The invention is provided with a corresponding temperature compensation system, ensures the optimal temperature of microorganism metabolism, can achieve the aim of efficiently purifying waste gas, and meets the actual use requirement.
Description
Technical Field
The invention relates to a microbial waste gas purification device, and belongs to the technical field of waste gas purification treatment.
Background
With the development of economy, the problem of exhaust pollution such as malodor has been more and more emphasized. Taking malodorous gases as an example, the malodorous gases can be divided into two main categories: one is an organic pollutant gas and the other is an inorganic gas. The organic pollution gas mainly comprises hydrocarbons and thiols, and the inorganic gas mainly comprises sulfide, ammonia compounds and the like. The gases have the characteristics of complex components and high treatment difficulty, and particularly some long-chain macromolecular substances have poor water solubility and are difficult to biodegrade. With the further research and development of microorganisms in the field of pollution control, the utilization of microorganisms has deeper research and practice in the aspect of treating air pollutants, and the main principle of purifying air by a microbial method is to degrade harmful substances in the air by utilizing the assimilation of a microbial population which is widely distributed, vigorous in metabolism, rapid in propagation and beneficial to application, so as to achieve the purpose of purifying the air. The technical scheme adopted by the prior art is as follows: waste gas enters the purifier from the middle air duct on the side surface of the purifier, and high-efficiency biological fillers with basically consistent thickness are paved on the upper layer and the lower layer of the air inlet duct. After entering the purifier, the waste gas is divided into two parts for simultaneous treatment. One part is purified simultaneously by the filler on the upper layer of the air inlet duct and the other part is purified simultaneously by the filler under the air inlet duct, so that the effects of one air inlet, simultaneous biological treatment of the two layers of fillers and simultaneous air exhaust after treatment are achieved. The function of the equipment is equivalent to that of the traditional two-stage equipment. Because only one air inlet is provided, two layers of air outlets are processed simultaneously, thus greatly reducing the occupied area of the equipment. Meanwhile, the contact area of the waste gas and the biological filler is greatly increased due to the large area of the filler, so that the treatment efficiency of the equipment can be greatly improved. Meanwhile, the ventilation area is large, and the air outlet is large, so that the resistance of waste gas passing through the equipment can be obviously reduced. The upper and lower two layers of fillers are fixed with high-efficiency strains for specially treating the waste gas. When the waste gas passes through the filler, a large number of microorganisms on the filler can capture and transmit pollutants in the waste gas into biological cells for degradation and purification, the pollutants are converted into nontoxic, odorless and harmless substances, such as carbon dioxide and water, and the purified waste gas is discharged to the atmosphere.
Although the prior art improves the gas purification effect to a certain extent, the prior art does not have good temperature control for microbial growth and metabolism, the temperature of the environment is required, the optimal effect of microbial purification can be exerted only at the optimal temperature, when a large amount of gas passes through, harmful components in the gas are difficult to be completely purified, and the discharged gas contains a large amount of moisture and strains, so that the waste gas treatment effect is inevitably reduced. For this reason, a corresponding technical scheme needs to be designed for solution.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides the microbial waste gas purification device which is provided with the corresponding temperature compensation system, so that the optimal temperature of microbial metabolism is ensured, the aim of efficiently purifying waste gas is fulfilled, and the actual use requirement is met.
In order to solve the problems, the technical scheme adopted by the invention is as follows:
the utility model provides a little waste gas purification device comprises fan, multi-stage filtration system, air-supply line, little biological purification device includes according to the order from left to right in proper order: a facultative anaerobic precipitation zone, a buffer zone, an aerobic zone, a drying adsorption layer, a sterilization zone and an exhaust pipe; the microbial purification device is characterized in that a liquid storage layer is arranged at the top of the microbial purification device, a spraying system matched with a facultative anaerobic precipitation area and an aerobic area is arranged in the liquid storage layer, and a temperature compensation system matched with the spraying system is arranged on the facultative anaerobic precipitation area and the aerobic area.
As an improvement of the above technical solution, the temperature compensation system includes: the temperature compensation chamber is internally provided with an inert gas inlet, a multifunctional sensor, a drainage unit, a temperature regulation unit and an inert gas outlet, wherein the multifunctional sensor is arranged in the temperature compensation chamber and is positioned in the facultative anaerobic precipitation zone and the aerobic zone
As an improvement of the above technical solution, the spraying system includes: one end of the spraying pipe is connected with the liquid storage layer, the spraying pipe is provided with a spraying pump, and the right sides of the facultative anaerobic precipitation zone and the aerobic zone are provided with a plurality of spraying nozzles and connected with the other end of the spraying pipe.
As an improvement of the technical scheme, the fan is arranged at the front end of the multistage filtering system, the multistage filtering system sequentially comprises a solid particle filtering layer, an organic matter filtering layer, a pebble layer and a flow equalizing layer from left to right, the flow equalizing layer is a baffle with holes, and the baffle is arranged in a baffling manner in a vertically staggered manner.
As an improvement of the technical scheme, the facultative anaerobic settling zone is filled with vertical materials, the aerobic zone is filled with horizontal materials, and the aerobic zone is also provided with an aeration system.
As an improvement of the technical scheme, the sterilization area is positioned in the drying adsorption layer, the drying adsorption layer is filled with drying agents and adsorbents, one end in the horizontal direction is provided with an opening for the gas to pass through in a single direction, and the outside of the drying adsorption layer is connected with the exhaust pipe.
As an improvement of the technical scheme, a gas backflow valve is arranged in the exhaust pipe, a gas density sensor used in a matched mode is arranged in the gas backflow valve, and a backflow pipeline communicated with the fan is connected to the gas backflow valve.
Compared with the prior art, the invention has the following implementation effects:
1. the invention realizes the adsorption and decomposition of harmful substances in the waste gas, wets the gas, brings enough moisture for microorganisms in a facultative anaerobic precipitation zone and an aerobic zone, and improves the decomposition efficiency.
2. The invention is provided with a temperature compensation system which controls the temperature of the nutrient solution, when the gas passes through, the temperature compensation system can sense whether the environmental temperature is suitable for the microorganism in time to make corresponding temperature adjustment, thereby leading the microorganism in the purification system to be at the most suitable temperature, leading the metabolism to be most active and leading the purification efficiency to be optimal.
3. The working efficiency of the facultative anaerobic sedimentation zone and the aerobic zone arranged in the invention is equivalent to that of two sets of traditional microbial purifiers, and the vertical and horizontal packing layers are added, so that the waste gas treatment efficiency and treatment capacity are improved.
4. The invention is provided with a corresponding return pipeline, and realizes the secondary purification process of the waste gas which is not purified completely until the purification treatment is complete.
5. The invention integrates adsorption, filtration and decomposition into a whole, has simple and convenient device structure, easy operation, small occupied area, space saving, good waste gas treatment efficiency and large amount.
Drawings
FIG. 1 is a schematic structural view of a microbial waste gas purification apparatus according to the present invention;
fig. 2 is a schematic structural diagram of the temperature compensation system according to the present invention.
Detailed Description
The present invention will be described with reference to specific examples.
Example (b): the utility model provides a little waste gas purification device, comprises fan 1, multistage filtration system 2, air-supply line 3, little biological purification device 4, and little biological purification device 4 includes in proper order from the left right side: a facultative anaerobic precipitation zone 41, a buffer zone 42, an aerobic zone 43, a dry adsorption layer 44, a sterilization zone 45, and an exhaust pipe 46; a liquid storage layer 47 is arranged at the top of the microbial purification device 4, and a spraying system matched with the facultative anaerobic precipitation zone 41 and the aerobic zone 43 is arranged in the liquid storage layer 47; the spraying system comprises: one end of the spraying pipe 61 is connected with the liquid storage layer 47, the spraying pipe 61 is provided with a spraying pump 62, the right sides of the facultative anaerobic precipitation zone 41 and the aerobic zone 43 are respectively provided with a plurality of spraying nozzles 63 and are connected with the other end of the spraying pipe 61, and the facultative anaerobic precipitation zone 41 and the aerobic zone 43 are provided with temperature compensation systems 50 used by matching with the spraying systems; the temperature compensation system 50 includes: the temperature compensation chamber 51 is internally provided with an inert gas inlet 52, a multifunctional sensor 53, a drainage unit 54, a temperature adjusting unit 55 and an inert gas outlet 56, wherein the multifunctional sensor 53 is arranged in the temperature compensation chamber 51 and is positioned in the facultative anaerobic precipitation zone 41 and the aerobic zone 43. The invention is provided with a temperature compensation system which controls the temperature of the nutrient solution, when the gas passes through, the temperature compensation system can sense whether the environmental temperature is suitable for the microorganism in time to make corresponding temperature adjustment, thereby leading the microorganism in the purification system to be at the most suitable temperature, leading the metabolism to be most active and leading the purification efficiency to be optimal. In addition, the facultative anaerobic sedimentation area and the aerobic area are arranged, the working efficiency is equivalent to two sets of traditional microbial purifiers, and the vertical and horizontal packing layers are added, so that the waste gas treatment efficiency and the treatment capacity are improved. The invention integrates adsorption, filtration and decomposition into a whole, has simple and convenient device structure, easy operation, small occupied area, space saving, good waste gas treatment efficiency and large amount.
Further improved, as shown in fig. 1: fan 1 locates 2 front ends of multi-stage filtration system, multi-stage filtration system 2 includes solid particle filter layer 21 in proper order according to from left to right in proper order and is arranged in adsorbing the solid-state particulate matter that mingles with in the waste gas, organic matter filter layer 22, cobble layer 23 and the layer 24 that flow equalizes, the layer 24 that flow equalizes is foraminiferous baffle, and the baffle is dislocation from top to bottom and sets up to the baffling form, mainly used realizes balanced distribution effect to the waste gas through prefilter, improves subsequent purification treatment efficiency.
Specifically, as shown in fig. 1: the facultative anaerobic settling zone 41 is filled with vertical materials 411, the aerobic zone 43 is filled with horizontal materials 431, the aerobic zone 43 is also internally provided with an aeration system 432, the vertical materials 411 and the horizontal materials 431 provide a better microbial growth environment under the cooperation of the temperature compensation system 50, and the optimal purification efficiency of microbes is realized; the sterilization area 45 is located in the dry adsorption layer 44, the dry adsorption layer 44 is filled with a drying agent and an adsorbent, and one end of the horizontal direction is provided with an opening for the unidirectional passage of air and is externally connected with an exhaust pipe 46.
More specifically, a gas backflow valve 70 is arranged in the exhaust pipe 46, a gas density sensor 71 which is used in cooperation is arranged in the gas backflow valve 70, a backflow pipeline 72 which is communicated with the fan 1 is connected to the gas backflow valve 70, for uncleaned waste gas, the density of the uncleaned waste gas is larger than that of the purified waste gas, when the uncleaned waste gas passes through the gas backflow valve 70, the gas density sensor 71 of the uncleaned waste gas can sense and realize signal transmission to open the gas backflow valve 70, and the uncleaned waste gas can reenters the fan 1 along the backflow pipeline 72 to realize the purification process.
The foregoing is a detailed description of the invention with reference to specific embodiments, and the practice of the invention is not to be construed as limited thereto. For those skilled in the art to which the invention pertains, several simple deductions or substitutions can be made without departing from the spirit of the invention, and all shall be considered as belonging to the protection scope of the invention.
Claims (7)
1. A microbial exhaust gas purification device, characterized in that: by fan (1), multistage filtration system (2), air-supply line (3), microorganism purifier (4) constitute, microorganism purifier (4) include according to the order from left to right in proper order: a facultative anaerobic precipitation zone (41), a buffer zone (42), an aerobic zone (43), a dry adsorption layer (44), a sterilization zone (45) and an exhaust pipe (46); microbial purification device (4) top is equipped with liquid storage layer (47), be equipped with the spray system that cooperation facultative anaerobic settling area (41) and aerobic zone (43) used in liquid storage layer (47), be equipped with temperature compensation system (50) that cooperation spray system used on facultative anaerobic settling area (41) and aerobic zone (43).
2. The microbial exhaust gas purification apparatus according to claim 1, characterized in that: the temperature compensation system (50) comprises: the temperature compensation chamber (51), be equipped with inert gas import (52), multi-functional sensor (53), drainage unit (54), temperature regulation unit (55) and inert gas discharge port (56) in the temperature compensation chamber (51), multi-functional sensor (53) set up in temperature compensation chamber (51) and be located facultative anaerobic sedimentation district (41) and aerobic district (43) inside
3. The microbial exhaust gas purification apparatus according to claim 1, characterized in that: the spraying system comprises: one end of the spraying pipe (61) is connected in the liquid storage layer (47), a spraying pump (62) is installed on the spraying pipe (61), and a plurality of spraying nozzles (63) are arranged on the right sides of the facultative anaerobic settling area (41) and the aerobic area (43) and connected with the other end of the spraying pipe (61).
4. The microbial exhaust gas purification apparatus according to claim 1, characterized in that: multistage filtration system (2 front ends) are located in fan (1), multistage filtration system (2) include solid particle filter layer (21), organic matter filter layer (22), cobble layer (23) and layer (24) flow equalizes according to from left right order in proper order, layer (24) flow equalizes is foraminiferous baffle, just the baffle is dislocation from top to bottom and sets up to the baffling form.
5. The microbial exhaust gas purification apparatus according to claim 3, characterized in that: the facultative anaerobic settling zone (41) is filled with vertical materials (411), the aerobic zone (43) is filled with horizontal materials (431), and the aerobic zone (43) is also internally provided with an aeration system (432).
6. The microbial exhaust gas purification apparatus according to claim 1, characterized in that: the sterilizing area (45) is located in the drying adsorption layer (44), the drying adsorption layer (44) is filled with drying agents and adsorbents, one end of the horizontal direction is provided with an opening, and the air is supplied to the air to pass through in a single direction and is connected with the exhaust pipe (46) from the outside.
7. The microbial exhaust gas purification apparatus according to claim 6, characterized in that: be equipped with gas return valve (70) in blast pipe (46), be equipped with gas density sensor (71) that the cooperation was used in gas return valve (70), be connected with backflow pipeline (72) with fan (1) intercommunication on gas return valve (70).
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CN201911034652.6A CN110624397A (en) | 2019-10-29 | 2019-10-29 | Microbial waste gas purification device |
PCT/CN2020/122702 WO2021083024A1 (en) | 2019-10-29 | 2020-10-22 | Microbial waste gas purification apparatus |
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CN201911034652.6A CN110624397A (en) | 2019-10-29 | 2019-10-29 | Microbial waste gas purification device |
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Cited By (2)
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WO2021083024A1 (en) * | 2019-10-29 | 2021-05-06 | 淮阴师范学院 | Microbial waste gas purification apparatus |
CN113413755A (en) * | 2021-07-22 | 2021-09-21 | 重庆市机电设计研究院 | Working system and working method for treating VOC (volatile organic compounds) through biological method |
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CN113019003B (en) * | 2021-05-25 | 2021-08-20 | 中农恒基现代农业产业研究院(诸城)有限公司 | Waste gas shock treatment facility is bred to oxygen-rich formula of heat accumulation |
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