CN207153435U - Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit - Google Patents
Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit Download PDFInfo
- Publication number
- CN207153435U CN207153435U CN201720925244.XU CN201720925244U CN207153435U CN 207153435 U CN207153435 U CN 207153435U CN 201720925244 U CN201720925244 U CN 201720925244U CN 207153435 U CN207153435 U CN 207153435U
- Authority
- CN
- China
- Prior art keywords
- processing unit
- container
- biological
- collecting tank
- exhaust gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- 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
- Treating Waste Gases (AREA)
Abstract
The utility model proposes a kind of container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit, it is related to the technical field of exhaust treating purifier.The utility model includes container, and the inside of container is provided with reaction of low temperature plasma device and biological treatment tower；Biological treatment tower includes tower body, the inside of tower body is provided with vertically arranged sieve plate, the centre of sieve plate is provided with sieve aperture, the both ends of sieve plate are sealed set, and the side of sieve plate is provided with pretreatment unit, and the opposite side of sieve plate is provided with biological processing unit, the bottom of tower body is additionally provided with collecting tank, the top of tower body is provided with spray equipment, and spray equipment is connected with collecting tank, and the flow direction of liquid of the gas flow direction with being sprayed out in spray equipment is intersected.The utility model in the inside of container, can integrally carry reaction of low temperature plasma device and biological treatment tower combination settings, and biological treatment tower carries out mass transfer by the way of gas and liquid cross-flow, easy for installation, start fast, and treatment effeciency is high.
Description
Technical field
The technical field of waste gas treatment equipment is the utility model is related to, particularly relates to a kind of container-type difficult degradation organic waste
Gas plasma and life assemblage method processing unit.
Background technology
Organic exhaust gas wide material sources, petrochemical industry, coking are mostly come from, printing and dyeing, sprays and the industry such as butchers, its is main
Processing mode includes absorption, catalysis oxidation and biological treatment etc..Wherein, absorption method is to utilize absorption of the adsorbent to organic principle
Characteristic reaches the purpose of physical separation, and this method is easy to operate, efficiency high, still, because its adsorption capacity is certain, need to be desorbed and locate again
Reason, therefore operating cost is higher；In addition, because of its own feature, existing equipment mainly handles low-concentration organic exhaust gas.Catalytic oxidation
It is by catalyst and is aided with suitable humiture and makes organic principle in waste gas that oxidation Decomposition occur and reach the mesh of exhaust-gas treatment
, the purification of this method is thorough, safe, however, the technological requirement is strict, exhaust gas constituents require harsh, once difference
Treatment effeciency will be largely effected on, in addition, the catalyst used in the technique is expensive.
Biological treatment is that the organic principle degraded using microorganism under control environment in waste gas realizes self procreation, dimension
Hold and grow and be translated into the process of carbon dioxide, water and other inorganic compounds, only need to feed a little nutrient in operation
With water.Therefore, Comparatively speaking, biological treatment is not only invested low with operating cost, moreover, management is convenient；It is but biological
The waste gas of facture processing needs good water solubility and can be degraded by microorganisms.Lower temperature plasma technology is produced substantial amounts of using electric discharge
O3、OH、H2O2Reacted Deng particle and high energy electron with organic exhaust gas molecule, it is resolved into small molecule or inorganic compound；
Its advantage is that the organic exhaust gas composition that can be decomposed is extensive, strong antijamming capability, still, can be produced after processing cost height and decomposition
Harmful side product.
The content of the invention
The purpose of this utility model is proposed at a kind of container-type difficult degradation organic exhaust gas plasma and life assemblage method
Device is managed, emission-control equipment of the prior art is solved and has that complicated, installation period is long, processing cost is high and difficult drop
Solve the halfway problem of VOCs treatment.
What the technical solution of the utility model was realized in：Including container, first is respectively equipped with the container
Air inlet and the first gas outlet, the inside of the container are provided with reaction of low temperature plasma device and biological treatment tower, and described
One air inlet is connected with admission line, and the other end of the admission line is connected with the reaction of low temperature plasma device, described
The output end of reaction of low temperature plasma device is connected with the biological treatment tower, and the output end of the biological treatment tower is connected with out
Feed channel, the outlet pipe are connected with first gas outlet；The biological treatment tower includes tower body, the side of the tower body
Provided with the second air inlet, the tower body is provided with the second gas outlet, the tower body on another relative side of the second air inlet
Inside be provided with vertically arranged sieve plate, the centre of the sieve plate is provided with sieve aperture, and the both ends of the sieve plate are sealed set, described
The side of sieve plate is provided with pretreatment unit, and the pretreatment unit is connected with second air inlet, the opposite side of the sieve plate
Provided with biological processing unit, the biological processing unit is connected with second gas outlet, and the bottom of the tower body is provided with liquid collecting
Groove, the top of the tower body are provided with spray equipment, and the spray equipment is connected with the collecting tank, the flow direction of gas and institute
Intersect the flow direction for stating the liquid sprayed out in spray equipment.
As a kind of preferred embodiment, the first filler is provided with the pretreatment unit, first filler is gold
Belong to any one or a few in silk screen, polyhedron empty ball, Raschig ring, saddle ring, the biological processing unit is biofiltration
Unit or bio-trickling unit, the biofiltration unit is interior to be provided with filter packing, and drop filter is provided with the bio-trickling unit
Biological membranous layer is equipped with filler, the filter packing and the drop filter filler.
As a kind of preferred embodiment, the biological membranous layer is the function mycoderm of activated sludge film layer or factory's culture
Layer, the filter packing be woven wire, polyhedron empty ball, volcanic rock, charcoal, haydite, in corrugated plating any one or
It is several, the drop filter filler is pottery material, volcanic rock, bamboo charcoal, bark, wood chip, compost, leaf mould, in turf any one or
It is several.
As a kind of preferred embodiment, the spray equipment includes spray pipeline and spray head, the spray pipeline
Bottom be connected by spray pump with the collecting tank, the spray head includes the first spray head above the pretreatment unit
With the second spray head above biological processing unit, the collecting tank includes the first liquid collecting positioned at pretreatment unit bottom
Groove and the second collecting tank positioned at biological processing unit bottom.
As a kind of preferred embodiment, the bottom of first collecting tank and second collecting tank is respectively equipped with confession
The socket that the car wall of fork truck penetrates.
As a kind of preferred embodiment, primary heater, the first temperature sensor are provided with first collecting tank
With the first pH value detector, second collecting tank is interior to be provided with secondary heater, second temperature sensor and the detection of the second pH value
Device.
As a kind of preferred embodiment, the bottom of the tower body is provided with the packing support plate laterally set, the tower
The bottom of observation window, feeding port and discharge port, the bottom of first collecting tank and second collecting tank is further respectively had on body
Portion is equipped with sewage draining exit and feed liquid adding mouth.
As a kind of preferred embodiment, the reaction of low temperature plasma device includes reactor body, the reaction
Device body is connected with high voltage power supply, and the front end of the reactor body is additionally provided with dust processor.
As a kind of preferred embodiment, the reaction of low temperature plasma device by check-valves and burning-point valve with it is described
Admission line connects, and the output end of the reaction of low temperature plasma device also is provided with check-valves.
As a kind of preferred embodiment, the reaction of low temperature plasma device is 1, and the biological treatment tower is 2-
3, for the biological treatment tower to be connected in series, the outlet pipe is provided with blower fan.
Compared with prior art, the beneficial effects of the utility model are：The utility model is by reaction of low temperature plasma device
With biological treatment tower combination settings in the inside of container, there is container protection outside, and transport and carrying are more convenient；Difficult degradation
Organic exhaust gas resolves into soluble in water, degradable lower-molecular substance or inorganic chemical after reaction of low temperature plasma device
Thing, then, into biological treatment tower in complete pretreatment and biological treatment, under the mating reaction of spray equipment and collecting tank,
Realize batch production processing and fabricating, live Fast Installation；Biological treatment tower of the present utility model is passed using gas and liquid cross-flow
The form of matter, gas carry out transverse horizontal motion, and through biological treatment tower, liquid realizes vertical spray from the top down, makes waste gas
In harmful components absorbed and dissolved, treatment effeciency is high；The processing unit characteristics of compact layout, start it is fast, be particularly suitable for containing
The processing of the organic exhaust gas of composition such as water, the polycyclic aromatic hydrocarbon of difficult for biological degradation, halogenated hydrocarbons, organonitrile compound is insoluble in, is handled
Gas meets environmental requirement afterwards, can be immediately discharged to air.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, is not paying the premise of creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the planar structure schematic diagram of the utility model one embodiment；
Fig. 2 is Fig. 1 overlooking the structure diagram；
Fig. 3 is the planar structure schematic diagram of biological treatment tower in Fig. 1；
Fig. 4 is Fig. 3 side structure schematic view；
Fig. 5 is the planar structure schematic diagram of sieve plate in Fig. 3；
In figure：1- containers；2- reaction of low temperature plasma devices；3- admission lines；4- spray pumps；5- pretreatment units；
6- biological processing units；7- biological treatment towers；8- outlet pipes；9- blower fans；10- switch boards；11- packing support plates；701-
Two air inlets；The fillers of 702- first；703- spray pipelines；The spray heads of 704- first；705- sieve plates；The spray heads of 706- second；
The fillers of 707- second；The gas outlets of 708- second；709- sockets；The collecting tanks of 710- second；The collecting tanks of 711- first；712- fillers
Mouthful；713- discharge ports；714- sieve apertures；715- blind ends.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
Refering to accompanying drawing 1, accompanying drawing 2, accompanying drawing 3, accompanying drawing 4 and accompanying drawing 5, the utility model includes container 1, divides on container 1
Not She You the first air inlet and the first gas outlet, the inside of container 1 is provided with reaction of low temperature plasma device 2 and biological treatment tower
7, the first air inlet is connected with admission line 3, and the other end of admission line 3 is connected with reaction of low temperature plasma device 2, low temperature etc.
The output end of plasma reactor 2 is connected also by admission line 3 with biological treatment tower 7, the output end connection of biological treatment tower 7
There is outlet pipe 8, outlet pipe 8 is connected with the first gas outlet；Reaction of low temperature plasma device 2 and biological treatment tower 7 are arranged on
The inside of container 1, make there is container 1 to protect outside it, it is more convenient to transport and carry, and pending waste gas is by the first air inlet
Mouthful enter admission line 3, after reaction of low temperature plasma device 2 and the processing of biological treatment tower 7, into outlet pipe 8 by
Discharge the first gas outlet；Biological treatment tower 7 includes tower body, and the side of tower body is provided with the second air inlet 701, and tower body is in the second air inlet
701 another relative side of mouth are provided with the second gas outlet 708, and the bottom of tower body is provided with the packing support plate laterally set
11, the inside of tower body is provided with vertically arranged sieve plate 705, and the centre of sieve plate 705 is provided with sieve aperture 714, and the both ends of sieve plate 705 are close
Envelope setting forms blind end 715, and the side of sieve plate 705 is provided with pretreatment unit 5, and pretreatment unit 5 connects with the second air inlet 701
Connect, the opposite side of sieve plate 705 is provided with biological processing unit 6, and biological processing unit 6 is connected with the second gas outlet 708, the bottom of tower body
Portion is provided with collecting tank, and the top of tower body is provided with spray equipment, and spray equipment is connected with collecting tank, the flow direction of gas and spray
Intersect the flow direction of the liquid sprayed out in device.Transverse movement of the gas along biological treatment tower 7, liquid is from biological treatment
The top down flowing of tower 7, gas and liquid form a kind of cross-flow；After difficult degradation organic exhaust gas enters container 1, first pass through low
Isothermal plasma reactor 2 carries out degradation treatment, and pretreatment and biological treatment are then completed in biological treatment tower 7, is being sprayed
Under the collective effect of device and collecting tank, batch production processing and fabricating is realized, live Fast Installation, starts quick, treatment effeciency
Height, gas meets environmental requirement after processing, can be immediately discharged to air.
Be provided with the first filler 702 refering to accompanying drawing 1 and accompanying drawing 4, in pretreatment unit 5, the first filler 702 be woven wire,
Any one or a few in polyhedron empty ball, Raschig ring, saddle ring, biological processing unit 6 is biological filter element or biology
Drop filter unit, biofiltration unit is interior to be provided with filter packing, drop filter filler is provided with bio-trickling unit, filter packing is filtered with drop
Filler is referred to as the second filler 707, and filter packing and drop filter filler are to be equipped with biological membranous layer on the second filler 707.First fills out
Material 702 is the larger medium of gas area of passage, and generally specific surface area is less than 100m2/ g inorganic filler, biological membranous layer are
Activated sludge film layer or the function bacterium film layer of factory's culture, the function bacterium film layer such as desulfurization mycoderm or de- hydrocarbon flora film of factory's culture
Layer, the microorganism of this biological membranous layer are screened in the environment or in the microorganism in sewage farm, this microbe survival energy
Power is strong, and need to only put into a small amount of nutritional agents early stage self can be multiplied by absorbing waste gas.Filter packing is woven wire, multiaspect sky
Any one or a few in bulbus cordis, volcanic rock, charcoal, haydite, corrugated plating, drop filter filler is pottery material, volcanic rock, bamboo charcoal,
Any one or a few in bark, wood chip, compost, leaf mould, turf；Filter packing be using strengthen gas-liquid contact chance and
The big material of biological bearing capacity is made, and generally specific surface area is in 250-400m2Inorganic filler between/g；Drop filter is filled out
Material is to use to have gas that very strong interception capacity, bearing microorganism ability are strong, can provide part nutrient source for microbial survival
Material or above combination of materials be made；These specific surface areas of the second filler 707 are big, and biomembrane Yi Shengyi falls, corrosion resistant
Erosion, resistance to biodegradation, humidity-preserving type is good, and porosity is big, and crushing is small, and gas distribution water distribution is good.
Refering to accompanying drawing 1 and accompanying drawing 4, spray equipment includes spray pipeline 703 and spray head, and the bottom of spray pipeline 703 leads to
Cross spray pump 4 to be connected with collecting tank, spray head is included positioned at the first spray head 704 of the top of pretreatment unit 5 and positioned at biology
Second spray head 706 of the top of processing unit 6, the envelope that the first spray head 704 and the second spray head 706 pass through the top of sieve plate 705
Closed end 715 is isolated, and collecting tank is included positioned at the first collecting tank 711 of the bottom of pretreatment unit 5 and positioned at the bottom of biological processing unit 6
Second collecting tank 710 in portion, the first collecting tank 711 and the second collecting tank 710 are isolated by the blind end 715 of the bottom of sieve plate 705.
Primary heater, the first temperature sensor and the first pH value detector are provided with first collecting tank 711, in the second collecting tank 710
Provided with secondary heater, second temperature sensor and the second pH value detector.The pretreatment unit 5 of this set and biological treatment
Unit 6 is separate, can add different liquid to be sprayed in different collecting tanks respectively, and to different collecting tanks
Implement different control, so as to the situation of waste gas in the situation and processing procedure according to pending waste gas, adjust different collection
The liquid of liquid bath and its spray temperature, the liquid circulation in collecting tank use, detect the pH value of liquid collecting tank liquid in good time, work as pH
After value exceeds preset range, a part of new liquid is replaced in time, to complete the replacing of liquid collecting tank liquid.The bottom of tower body is set
There is the packing support plate 11 laterally set, packing support plate 11 is used to support the first filler 702 and the second filler 707, filler branch
Fagging 11 is formed using fiberglass Turbogrid plates and Dense mesh screen, and packing support plate 11 is respectively positioned at the first collecting tank 711 and the second collection
The top of liquid bath 710, the first filler 702 and the second filler 707 are respectively positioned on the lower section of spray equipment, and sight is further respectively had on tower body
Examine window, feeding port 712 and discharge port 713, the bottom of the bottom of the first collecting tank 711 and the second collecting tank 710 is equipped with blowdown
Mouth and feed liquid adding mouth；In the present embodiment, feeding port 712 is located at the top of tower body, facilitates the addition of filler, discharge port 713
In the side of tower body, to facilitate the discharging of filler；Generally, a feeding port 712 and two is set on each processing unit
Individual discharge port 713, to facilitate the addition of filler and discharging.Sewage draining exit can discharge sludge in time, and feed liquid adding mouth can be timely
Fresh liquid is supplemented, sewage draining exit and feed liquid adding mouth are also independent control, make the first collecting tank 711 and the second collecting tank
710 are completely independent, and are easy to control.
Refering to accompanying drawing 1 and accompanying drawing 4, the bottom of the first collecting tank 711 and the second collecting tank 710 is respectively equipped with the car for fork truck
The socket 709 that wall penetrates.The setting of socket 709, facilitate the carrying of biological treatment tower 7, it is assembled simple and fast.The present embodiment
In, reaction of low temperature plasma device 2 is 1, and biological treatment tower 7 is 2,2 biological treatment towers 7 pass through to be connected in parallel
Difficult degradation organic waste qi leel two-way after the processing of reaction of low temperature plasma device 2 respectively enters biological treatment tower 7, at biology
Reason tower 7 is discharged after handling by outlet pipe 8, and outlet pipe 8 is provided with blower fan 9, and blower fan 9 is by two-way by biological treatment tower 7
The gas sampling of reason is discharged to concentration after bellows；Certainly, on each exhaust-gas treatment pipeline, biological treatment tower 7 can also be 2-3
Individual, this 2-3 biological treatment tower 7 is is connected in series, i.e., the difficult degradation organic waste after the processing of reaction of low temperature plasma device 2
Gas is continuously entered after 2-3 biological treatment tower 7 carries out 2-3 level processing and is then exhausted from.The utility model, switch board can also be installed
10, whole emission-control equipment is automatically controlled and is guarded by a PLC system, make its easy to control, accomplish timing monitoring, if
It is standby without personal management, it is daily it is basic do not have to safeguard, continuous operation in 24 hours, and be adapted to intermittent duty.
In addition, in the utility model, reaction of low temperature plasma device 2 includes reactor body, and reactor body is connected with
High voltage power supply, the front end of reactor body are additionally provided with dust processor.Difficult degradation organic exhaust gas goes gumming by dust processor
Enter reactor body after dirt, high voltage power supply forms electric discharge between discharge electrode and earthing pole, produces O3、OH、H2O2Etc. oxidisability
Strong active particle and high energy electron, reacted with difficult degradation organic exhaust gas, waste gas is resolved into soluble in water, degradable low point
Sub- material or inorganic compound；If having droplet or other aerosol particles in waste gas, they can catch electronics as itself electricity
Lotus, under electric field action, these band point particles will be attracted capture by electrode, so as to be separated from air-flow.Low-temperature plasma
Reactor according 2 is connected by check-valves and burning-point valve with admission line 3, and the output end of reaction of low temperature plasma device 2 also is provided with
Check-valves.The reaction of low temperature plasma device 2 controls easily, safe.
Exhaust-gas treatment principle：It is first after waste gas enters container 1 refering to the direction indicated by arrow in accompanying drawing 1 and accompanying drawing 3
First pass through admission line 3 and enter reaction of low temperature plasma device 2, after the processing of reaction of low temperature plasma device 2, divide two-way point
Not Jin Ru biological treatment tower 7, pass through pretreatment unit 5 and biological processing unit 6 successively in the inside of biological treatment tower 7, spray
Pump 4 will have been heated to the Liquid extracting of suitable temperature out of the bottom of biological treatment tower 7 the first collecting tank 711, and pass through spray
The top of pretreatment unit 5 is delivered on shower pipe road 703, by the uniform sprinkling of the first shower nozzle 704 on the first filler 702, spray
Liquid gradually passes through whole pretreatment unit 5 by the space of the first filler 702, after reaching ideal conditions, unnecessary moisture and molten
Exhaust gas recirculation in Xie Yushui is to the first collecting tank of bottom 711；Waste gas enters from the left side of pretreatment unit 5, with spray and under
Liquid into vertical direction by the first filler 702 after, enter biological processing unit 6 from the right side of pretreatment unit 5；Pretreatment
The main function of unit 5 is further removal dust granules, prevents dust is formed in subsequent biological treatment unit 6 from accumulating, because
Dust blocks the air-flow velocity that can reduce biological treatment tower 7 and increases windage；Meanwhile pretreatment unit 5 is also to the temperature of waste gas
Adjusted with humidity, component portion soluble in water in waste gas is dissolved, mitigate the load of subsequent biological treatment unit 6.
Biological processing unit 6 abuts against pretreatment unit 5, waste gas after washing pre-processes, temperature and humidity in the reasonable scope,
Contribute to the growth of microorganism, reach the requirement of microbial degradation, and in the surface biofilm of the second filler 707, microorganism
Harmful substance is swallowed in a short time and degraded；With the continuous continuous release by with biological respinse heat of gas, moisture
There is certain loss, now, the liquid sprayed by the second spray head 706 supplements biomembrane moisture in time, ensure that biological anti-
Should well it run；The effect of biological processing unit 6 mainly will be dissolvable in water the composition of water as far as possible from gas again in waste gas
Liquid phase is mutually transferred to, and is degraded by microbial biochemical, so as to complete the processing work of waste gas.
In the processing procedure of waste gas, the bottom of biological treatment tower 7 is provided with spray pipeline 703, can pass through the liquid of spray
Further adjust the humidity and temperature of different processing units；The liquid of spray uses the circulatory system, can recycle；Pretreatment is single
In member 5 liquid that sprays be to adjust temperature and humidity, in order to prevent air-flow take away partial moisture cause the water surface decline after gas
Body is altered the end to biological treatment tower 7 from lower space short circuit, and the liquid sprayed in biological processing unit 6 is effectively to be supplemented
, the liquid sprayed in biofiltration unit 6 is then to prevent that caused heat causes moisture evaporation to be subject in biodegradation process
Supply.
Compared with prior art, the beneficial effects of the utility model are：The utility model is by reaction of low temperature plasma device 2
With the combination settings of biological treatment tower 7 in the inside of container 1, outside has container 1 to protect, and it is more convenient to transport and carry；It is difficult
Degradation organic waste gas resolves into soluble in water, degradable lower-molecular substance or inorganic after reaction of low temperature plasma device 2
Compound, then, pretreatment and biological treatment are completed into biological treatment tower 7 is interior, is cooperated in spray equipment and matching somebody with somebody for collecting tank
Under, batch production processing and fabricating is realized, live Fast Installation, is started quick；Biological treatment tower 7 of the present utility model uses gas
The form of body and liquid cross-flow mass transfer, gas carry out transverse horizontal motion, and through biological treatment tower 7, liquid is realized from the top down
Vertical spray, makes the harmful components in waste gas be absorbed and dissolved, and treatment effeciency is high；The processing unit characteristics of compact layout, start
It hurry up, be particularly suitable for containing being insoluble in the organic of the compositions such as water, the polycyclic aromatic hydrocarbon of difficult for biological degradation, halogenated hydrocarbons, organonitrile compound
The processing of waste gas, gas meets environmental requirement after processing, can be immediately discharged to air.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc., the utility model should be included in
Protection domain within.
Claims (10)
1. a kind of container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit, it is characterised in that：Including collection
Vanning, is respectively equipped with the first air inlet and the first gas outlet on the container, the inside of the container be provided with low temperature etc. from
Daughter reactor and biological treatment tower, first air inlet are connected with admission line, the other end of the admission line and institute
The connection of reaction of low temperature plasma device is stated, the output end of the reaction of low temperature plasma device is connected with the biological treatment tower,
The output end of the biological treatment tower is connected with outlet pipe, and the outlet pipe is connected with first gas outlet；
The biological treatment tower includes tower body, and the side of the tower body is provided with the second air inlet, and the tower body is in the second air inlet
Another relative side is provided with the second gas outlet, and the inside of the tower body is provided with vertically arranged sieve plate, the sieve plate
Centre is provided with sieve aperture, and the both ends of the sieve plate are sealed set, and the side of the sieve plate is provided with pretreatment unit, the pretreatment
Unit is connected with second air inlet, and the opposite side of the sieve plate is provided with biological processing unit, the biological processing unit with
The second gas outlet connection, the bottom of the tower body are provided with collecting tank, and the top of the tower body is provided with spray equipment, the spray
Shower device is connected with the collecting tank, the flow direction of gas and the flow direction phase of the liquid sprayed out in the spray equipment
Hand over.
2. container-type difficult degradation organic exhaust gas plasma according to claim 1 and life assemblage method processing unit, its
It is characterised by：
The first filler is provided with the pretreatment unit, first filler is woven wire, polyhedron empty ball, Raschig ring, horse
Any one or a few in saddle ring, the biological processing unit are biological filter element or bio-trickling unit, the biology
Filter packing is provided with filter element, drop filter filler, the filter packing and the drop filter are provided with the bio-trickling unit
Biological membranous layer is equipped with filler.
3. container-type difficult degradation organic exhaust gas plasma according to claim 2 and life assemblage method processing unit, its
It is characterised by：
The biological membranous layer is the function bacterium film layer that activated sludge film layer or factory cultivate, the filter packing be woven wire,
Any one or a few in polyhedron empty ball, volcanic rock, charcoal, haydite, corrugated plating, the drop filter filler are pottery material, fire
Any one or a few in mountain rock, bamboo charcoal, bark, wood chip, compost, leaf mould, turf.
4. container-type difficult degradation organic exhaust gas plasma according to claim 1 and life assemblage method processing unit, its
It is characterised by：
The spray equipment includes spray pipeline and spray head, and the bottom of the spray pipeline passes through spray pump and the collecting tank
Connection, the spray head include the first spray head above pretreatment unit and second above biological processing unit
Spray head, the collecting tank include the first collecting tank positioned at pretreatment unit bottom and the positioned at biological processing unit bottom
Two collecting tanks.
5. container-type difficult degradation organic exhaust gas plasma according to claim 4 and life assemblage method processing unit, its
It is characterised by：
The bottom of first collecting tank and second collecting tank is respectively equipped with the socket penetrated for the car wall of fork truck.
6. container-type difficult degradation organic exhaust gas plasma according to claim 4 and life assemblage method processing unit, its
It is characterised by：
Primary heater, the first temperature sensor and the first pH value detector, second collection are provided with first collecting tank
Secondary heater, second temperature sensor and the second pH value detector are provided with liquid bath.
7. container-type difficult degradation organic exhaust gas plasma according to claim 5 and life assemblage method processing unit, its
It is characterised by：
The bottom of the tower body is provided with the packing support plate laterally set, and observation window, feeding port are further respectively had on the tower body
And discharge port, the bottom of the bottom of first collecting tank and second collecting tank are equipped with sewage draining exit and feed liquid adding mouth.
8. container-type difficult degradation organic exhaust gas plasma and life assemblage method according to any one in claim 1-7
Processing unit, it is characterised in that：
The reaction of low temperature plasma device includes reactor body, and the reactor body is connected with high voltage power supply, described anti-
The front end of device body is answered to be additionally provided with dust processor.
9. container-type difficult degradation organic exhaust gas plasma according to claim 8 and life assemblage method processing unit, its
It is characterised by：
The reaction of low temperature plasma device is connected by check-valves and burning-point valve with the admission line, the low-temperature plasma
The output end of reactor according also is provided with check-valves.
10. container-type difficult degradation organic exhaust gas plasma according to claim 1 and life assemblage method processing unit, its
It is characterised by：
The reaction of low temperature plasma device is 1, and the biological treatment tower is 2-3, and the biological treatment tower connects for series connection
Connect, the outlet pipe is provided with blower fan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720925244.XU CN207153435U (en) | 2017-07-27 | 2017-07-27 | Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720925244.XU CN207153435U (en) | 2017-07-27 | 2017-07-27 | Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207153435U true CN207153435U (en) | 2018-03-30 |
Family
ID=61714976
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720925244.XU Active CN207153435U (en) | 2017-07-27 | 2017-07-27 | Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207153435U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108786433A (en) * | 2018-05-07 | 2018-11-13 | 中国科学院过程工程研究所 | A kind of exhaust gas dust, waste liquid, exhaust gas coprocessing device and method |
| CN109499352A (en) * | 2018-11-27 | 2019-03-22 | 蓝天环保设备工程股份有限公司 | A kind of VOCs biological treatment device |
| CN111185081A (en) * | 2020-02-26 | 2020-05-22 | 广东新龙海洋装备科技有限公司 | Waste gas treatment device and waste gas treatment method |
| WO2020151545A1 (en) * | 2019-01-26 | 2020-07-30 | 苏州敬天爱人环境科技有限公司 | Plasma catalysis method and biological method-based organic waste gas treatment device |
| CN111974180A (en) * | 2020-06-17 | 2020-11-24 | 金华市中荷环保科技有限公司 | Large-scale reactor of low temperature plasma |
| CN113546517A (en) * | 2020-04-26 | 2021-10-26 | 上海双昊环保科技有限公司 | Integrated bio-trickling filtration waste gas treatment equipment |
-
2017
- 2017-07-27 CN CN201720925244.XU patent/CN207153435U/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108786433A (en) * | 2018-05-07 | 2018-11-13 | 中国科学院过程工程研究所 | A kind of exhaust gas dust, waste liquid, exhaust gas coprocessing device and method |
| CN108786433B (en) * | 2018-05-07 | 2020-09-18 | 中国科学院过程工程研究所 | Flue gas dust, waste liquid and waste gas co-treatment device and method |
| CN109499352A (en) * | 2018-11-27 | 2019-03-22 | 蓝天环保设备工程股份有限公司 | A kind of VOCs biological treatment device |
| WO2020151545A1 (en) * | 2019-01-26 | 2020-07-30 | 苏州敬天爱人环境科技有限公司 | Plasma catalysis method and biological method-based organic waste gas treatment device |
| CN111185081A (en) * | 2020-02-26 | 2020-05-22 | 广东新龙海洋装备科技有限公司 | Waste gas treatment device and waste gas treatment method |
| CN111185081B (en) * | 2020-02-26 | 2023-09-22 | 广东新龙海洋装备科技有限公司 | Exhaust gas treatment device and exhaust gas treatment method |
| CN113546517A (en) * | 2020-04-26 | 2021-10-26 | 上海双昊环保科技有限公司 | Integrated bio-trickling filtration waste gas treatment equipment |
| CN111974180A (en) * | 2020-06-17 | 2020-11-24 | 金华市中荷环保科技有限公司 | Large-scale reactor of low temperature plasma |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207153435U (en) | Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit | |
| CN102895867B (en) | Biochemical waste gas deodorization purification apparatus and biological deodorization method | |
| CN106039984B (en) | Sewage plant waste gas cleaning system based on pretreatment and biofilter group technology | |
| CN203507806U (en) | Ethylene oxide waste gas treatment device | |
| CN207137688U (en) | A kind of container-type VOCS and foul gas bioanalysis emission-control equipment | |
| CN103599695B (en) | A kind of integrated treating device of organic exhaust gas and method | |
| CN108211773A (en) | A kind of plural serial stage tandem type biology integrates deodorizing method and device | |
| CN202569951U (en) | Device for performing biological deodorization and waste gas treatment on sewage | |
| CN101496993A (en) | Method and device for processing malodorous gas by active bamboo charcoal-H2O2 complex phase catalytic oxidation | |
| CN108187466B (en) | Advanced oxidation coupling biological purification system based on ozone regulation and control and application thereof | |
| CN104147921B (en) | A kind of apparatus and method of the activated carbon combined method processing foul gas of biofiltration | |
| CA2160311A1 (en) | Method of extracting light volatile solvents from a gaseous effluent by wet-scrubbing a gaseous effluent and biomethanation of the solvent-rich liquid | |
| CN103801191B (en) | The equipment of biofiltration process foul smell and organic pollution | |
| CN203458937U (en) | Waste gas treatment device | |
| WO2021083024A1 (en) | Microbial waste gas purification apparatus | |
| CN205109392U (en) | Absorption process and biological method combined effect handle device of VOC waste gas | |
| CN108404648A (en) | A kind of microorganism waste gas purification apparatus | |
| CN206746308U (en) | A kind of exhaust air deodorization purifier | |
| CN203710909U (en) | Integrated treatment device of organic waste gas | |
| CN102688669A (en) | Waste gas purification plant with integration of plasma and biological method | |
| CN205598960U (en) | Be used for algae moisture stench waste gas pollution control and treatment device leaving from station | |
| CN204841388U (en) | Box VOC decomposes compound purification unit | |
| CN2844113Y (en) | Wet-land sewage-water treater of filter adsorptive submerge | |
| CN1743283B (en) | Filter-adsorption-submerged floating wet land sewage treating system and apparatus | |
| CN205627619U (en) | Modular biological deodorization UV clean system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |