CN207076344U - One kind purification equipment integrating and purification integrated system - Google Patents
One kind purification equipment integrating and purification integrated system Download PDFInfo
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- CN207076344U CN207076344U CN201720942709.2U CN201720942709U CN207076344U CN 207076344 U CN207076344 U CN 207076344U CN 201720942709 U CN201720942709 U CN 201720942709U CN 207076344 U CN207076344 U CN 207076344U
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- purification
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Abstract
The utility model proposes one kind purification equipment integrating and purification integrated system, including tower body, the tower body bottom to be provided with the first air inlet, and top is provided with the first gas outlet；It is bottom-up in the tower body to be sequentially provided with the first shower, ultra centrifugal layer, the ultra centrifugal layer includes supporting plate, the supporting plate is provided with some centrifugation disks, the centrifugation disk includes central block, the central block both sides are provided with screen pack, support bar is connected with the central block, the system selects whirlwind+eddy flow tower+spray+ultra centrifugal case and photodissociation plasma light catalyst container.Two tanks Combined Treatment all-in-one.It is effective to remove VOCs waste gas caused by blasting craft particulate matter and lacquer spraying technique section.It is expected that handling rate more than 90%, it is ensured that long-term efficiently up to standard.
Description
Technical field
It the utility model is related to field of environment protection equipment, more particularly to purification equipment integrating and purification integrated system.
Background technology
The method species of processing organic exhaust gas is various at present, and feature is different, thus the administering method accordingly used also it is each not
Identical, conventional has absorption process, direct combustion method, Production by Catalytic Combustion Process, absorption method etc..
1. absorption process
Absorption process can be divided into chemical absorbing and Physical Absorption, and most of organic exhaust gas should not use chemical absorbing.Physics is inhaled
Receipts require that absorbent should have and have higher affinity with absorbent components, low volatility, through parsing or rectifying after absorbing liquid saturation
After reuse.This law is suitable for the waste gas of middle and high concentration, but to select a kind of low volatility absorbing liquid of Cheap highly effective also to compare
It is more difficult, while secondary pollution problem is relatively difficult to resolve certainly, clean-up effect is undesirable.
2. direct combustion method
This law is also known as thermal oxidation method, flame combustion method, is the heat released using aid fuel combustions such as combustion gas or fuel oils
Mixed gas is heated to certain temperature (700~800 DEG C) by amount, is resident the regular hour (0.3~0.5 second), makes flammable to have
Evil material carries out pyrolytic and is changed into innocuous substance.
The characteristics of this law：Technique is simple, is applicable high-concentration waste gas administers；For itself aphlogistic middle low concentration tail
Gas, combustion adjuvant or heating are generally needed, energy consumption is greatly (operating cost is higher than Production by Catalytic Combustion Process more than 10 times)；Running technology requires high,
Whard to control and grasp.This method does not obtain popularization substantially at home, only a small number of producer's Introduced From Abroad abatement equipments be applied to compared with
In the tank tin graphed sheet industry waste gas pollution control and treatment processed of high concentration and temperature, but eventually because energy consumption is big and fluctuation of service, it is difficult to run well.
3. Production by Catalytic Combustion Process
The method is that waste gas is heated into 200~300 DEG C to burn by catalytic bed, reaches purification purpose.Its advantage is energy consumption
It is low, purifying rate is high, non-secondary pollution, technique simple operations are convenient.Combustible burns under catalyst action, with phase of directly burning
Than catalysis ignition temperature is relatively low, and ratio of combustion is more complete.Suitable for the VOCs treatment of high-temperature high concentration, it is not suitable for low dense
Degree, the VOCs treatment of Wind Volume.
4. absorption method
(1) direct active carbon adsorption
Organic exhaust gas can reach more than 90% purifying rate, equipment is simple, investment is small by the absorption of activated carbon.The method
The activated carbon of adsorption saturation can not be regenerated, it is desirable to often change activated carbon to ensure clean-up effect, cause to load and unload, transport
Secondary pollution is caused Deng during.
Utility model content
In order to solve the above technical problems, the utility model proposes one kind to purify equipment integrating, including tower body, the tower body
Bottom is provided with the first air inlet, and top is provided with the first gas outlet；It is bottom-up in the tower body to be sequentially provided with the first shower, surpass
Level centrifugation layer, the ultra centrifugal layer include supporting plate, and the supporting plate is provided with some centrifugation disks, the centrifugation
Disk includes central block, and the central block both sides are provided with screen pack, support bar is connected with the central block.
Preferably, it is connected with ring stiffener on the screen pack.
Preferably, the screen pack is disc-shaped structure, and the disc structure is provided with to be dissipated centered on central block and set
The steel wire put.
One kind purification integrated system, including purification equipment integrating, eddy flow tower, filtering photodissociation device, blower fan and aiutage, institute
Stating filtering photodissociation device includes shell, and the shell both ends are respectively equipped with the second air inlet and the second gas outlet, in the shell
Provided with primarily efficient filter layer and photodissociation layer；The primarily efficient filter layer is set on second air inlet, including housing, the housing
There are nonwoven layer, nylon wire, activated carbon filter material, metal hole pattern.
Preferably, the housing is paper frame, aluminium frame, zinc-plated chase.
Preferably, the photodissociation layer includes UV ultraviolet lamps, and active nano titanium oxide is provided between the UV ultraviolet lamps
Layer.
Preferably, the blower fan is connected to second gas outlet, and the aiutage, the row are connected with the blower fan
The high 20m of inflator.
Preferably, the eddy flow tower includes casing, water pump, and at least two second showers, institute are connected with the water pump
The second shower is stated to be located in the shell；The outer casing bottom is provided with eddy flow motor, is connected with the eddy flow motor some
Swirl vane.
Preferably, the tapered setting of the swirl vane, and conical lower portion is provided with blind plate, the swirl vane edge is provided with
Guiding gutter, mozzle is provided between the guiding gutter of adjacent swirl vane.
The utility model proposes a kind of purification equipment integrating and integral cleaning system have following beneficial effect：The system is selected
With whirlwind+eddy flow tower+spray+ultra centrifugal case and photodissociation plasma light catalyst container.Two tanks Combined Treatment all-in-one.Effectively
Remove VOCs waste gas caused by blasting craft particulate matter and lacquer spraying technique section.It is expected that handling rate more than 90%, it is ensured that long-term efficient
It is up to standard.
Brief description of the drawings
, below will be to needed for embodiment description in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
The accompanying drawing to be used is briefly described.
Fig. 1 is purification equipment integrating structural representation of the present utility model；
Fig. 2 is the schematic diagram of purification integrated system of the present utility model；
Fig. 3 is the schematic diagram of eddy flow tower of the present utility model；
Fig. 4 is the schematic diagram of ultra centrifugal layer of the present utility model；
Fig. 5 is the schematic diagram of filtering photodissociation device of the present utility model；
Fig. 6 is the schematic diagram of primarily efficient filter layer of the present utility model；
Wherein, 1- tower bodies, the air inlets of 2- first, the gas outlets of 3- first, the showers of 4- first, 5- ultra centrifugal layers, 6- branch
Fagging, 7- central blocks, 8- support bars, 9- steel wires, 10- ring stiffeners, 11- purification equipment integratings, 12- eddy flow towers, 13- filterings
Photodissociation device, 14- blower fans, 15- aiutages, 16- shells, the air inlets of 17- second, the gas outlets of 18- second, 19- primarily efficient filter layers,
20- photodissociation layers, 21- housings, 22- nonwoven layers, 23- nylon wires, 24- activated carbon filter materials, 25- casings, 26- water pumps, 27- second
Shower, 28- eddy flow motors, 29- mozzles, 30- swirl vanes, 31- blind plates.
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 describe.
As shown in figure 1, the utility model proposes one kind to purify equipment integrating, including tower body 1, the bottom of tower body 1 are set
There is the first air inlet 2, top is provided with the first gas outlet 3；Bottom-up the first shower 4, super of being sequentially provided with the tower body 1
Layer 5 is centrifuged, the ultra centrifugal layer 5 includes supporting plate 6, and the supporting plate 6 is provided with some centrifugation disks, the centrifugation point
Separation disc includes central block 7, and the both sides of central block 7 are provided with screen pack, support bar 8 are connected with the central block 7, wherein super
Centrifuge layer 5, be installed on motor, and 2300 revs/min at a high speed rotate when, formed physical shielding, can by the substantial amounts of grease of waste gas,
The solid phases such as dust, vapor, fiber, liquid phase substance are intercepted and separated by centrifugal principle, and gas can be passed through easily very much
Tiny steel wire 9 is taken.
Wherein, it is connected with ring stiffener 10 on the screen pack, the screen pack is disc-shaped structure, the disk knot
Structure is provided with the steel wire 9 that setting is dissipated centered on central block 7, and steel wire 9 itself is thinner, and intensity is relatively low, so there is provided annular
Reinforcement 10 is reinforced, while is connected central block 7 using support bar 8 and be supported.
One kind purification integrated system, including above-mentioned purification equipment integrating 11, eddy flow tower 12, filtering photodissociation device 13, wind
Machine 14 and aiutage 15, the filtering photodissociation device 13 include shell 16, and the both ends of shell 16 are respectively equipped with the second air inlet
17 and second gas outlet 18, primarily efficient filter layer 19 and photodissociation layer 20 are provided with the shell 16, and roughing efficiency air filter is applied to air-conditioning
The primary filter of system, it is mainly used in 5 μm of filtering with dust particles, roughing efficiency air filter there are board-like, collapsible, three kinds of samples of pocket type
Formula, the material of housing 21 have paper frame, aluminium frame, zinc-plated chase, and filtering material has non-woven fabrics, nylon wire 23, activated carbon filter material 24, metal
Hole pattern etc., protection network have two-sided plastic-spraying wire netting and double side zinc coating wire netting, are exactly the main reason for effect at the beginning of designing one layer here
Prevent centrifugation from failing, under the emergency situations do not discovered, just imitate can and play filtration, doing effect when centrifugation is,
Just imitate and do not work.Just active layer is exactly to play a part of a double insurance for design.
Wherein, the photodissociation layer 20 includes UV ultraviolet lamps, and active nano titanium oxide is provided between the UV ultraviolet lamps
Layer, after industrial waste gas is input to efficient photodissociation oxidation processes module using exhaust equipment, cleaning equipment uses high energy UV ultraviolets
Light beam and ozone carry out collaboration to waste gas and decompose oxidation reaction, change into the foul gas mass degradation in waste gas degraded
Compound, water and carbon dioxide, then outdoor is discharged by exhaust duct.Specifically, efficient photodissociation oxidation processes module utilizes height
The oxygen molecule that energy UV ultraviolet beams are decomposed in air produces free oxygen, i.e. active oxygen, because free oxygen takes positron-electron injustice
Weighing apparatus with oxygen molecule so need to be combined, and then produce ozone.Pre-Ozonation on Organic Matter has extremely strong oxidation, to foul gas and
Other excitant peculiar smell have the elimination effect to get instant result.
Efficient photodissociation oxidation processes module cracks effluvium using high energy high ozone UV ultraviolet beams irradiation foul gas
Ammonia, trimethylamine, hydrogen sulfide, first sulphur hydrogen, methyl mercaptan, methyl sulfide, methyl disulfide, carbon disulfide and styrene, sulfide in body
H2S, VOC class, the molecular link of benzene,toluene,xylene, make to be combined into small point with ozone oxidation in the contaminant molecule of free state
The compound of sub harmless or low evil, such as CO2, H2O.
Efficient photodissociation oxidation processes module is destroyed using bacteria molecule key in high energy UV ultraviolet beam cracking foul gas
The nucleic acid (DNA) of bacterium, then oxidation reaction is carried out by ozone, thoroughly reach deodorization and kill the purpose of bacterium, photocatalysis master
It is super high-activity nano titanium oxide to want composition, and inorganic nano material is nontoxic, and pure natural mineral modified, Detitanium-ore-type is received
Meter Jing Ti, it can promptly adsorb the simultaneously pernicious gas such as decomposing formaldehyde, benzene, toluene, ammonia, TVOC.Its main performance is that particle diameter is super
It is small, dispersive property is good, catalytic activity is high, cost-effective.
Preferably, the blower fan 14 is connected to second gas outlet 18, and the aiutage is connected with the blower fan 14
15, the 15 high 20m of aiutage.
Preferably, the eddy flow tower 12 includes casing 25, water pump 26, and at least two second sprays are connected with the water pump 26
Shower pipe 27, second shower 27 are located in the shell 16；The bottom of shell 16 is provided with eddy flow motor 28, the eddy flow
Some swirl vanes 30, the 30 tapered setting of swirl vane are connected with motor 28, and conical lower portion is provided with blind plate 31, institute
State the edge of swirl vane 30 and be provided with guiding gutter, mozzle 29, column plate blade are provided between the guiding gutter of adjacent swirl vane 30
Such as fixed air vane, produce rotation when air-flow passes through blade and centrifugal motion, absorbing liquid are uniformly divided by middle blind plate 31
Be fitted on blade, form thin liquid layer, the effect of rotation and centrifugation is formed with rotating upward air-flow, is sprayed into fine drop, get rid of to
After tower wall.Drop is flowed to collecting tank by Action of Gravity Field collection, and the area of blind plate 31 of next column plate is flowed to by downspout.With certain
Blast, the pending air-flow of wind speed enter from the bottom of tower, and top goes out.Absorbing liquid is entered from the top of tower, and bottom goes out.Air-flow is with absorbing
Liquid performs relative motion in tower, and the moisture film of the structure position formation very high surface area in the plate of eddy flow tower 12, so as to greatly improve
Absorption.Each layer of absorbing liquid falls into the collecting tank at edge through eddy flow centrifugal action, then next through the entrance of mozzle 29
Layer column plate, carry out next layer of absorption.
Rotational flow and spray tower is extracted with water by water pump 26 from water tank, and is recycled after filtering.Repeatedly after circulation
Sewage, it is i.e. recyclable after simple process to reuse.
A variety of modifications to embodiment will be apparent for those skilled in the art, determine herein
The General Principle of justice can be realized in other embodiments in the case where not departing from spirit or scope of the present utility model.Cause
This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein
The most wide scope consistent with features of novelty.
Claims (9)
1. one kind purification equipment integrating, it is characterised in that including tower body, the tower body bottom is provided with the first air inlet, and top is set
There is the first gas outlet；It is bottom-up in the tower body to be sequentially provided with the first shower, ultra centrifugal layer, the ultra centrifugal layer bag
Supporting plate is included, the supporting plate is provided with some centrifugation disks, and the centrifugation disk includes central block, the central block two
Side is provided with screen pack, and support bar is connected with the central block.
2. purification equipment integrating according to claim 1, it is characterised in that annular reinforcement is connected with the screen pack
Muscle.
3. purification equipment integrating according to claim 1, it is characterised in that the screen pack is disc-shaped structure, described
Disc structure is provided with the steel wire that setting is dissipated centered on central block.
4. one kind purification integrated system, it is characterised in that including the purification equipment integrating as described in any in claims 1 to 3,
Eddy flow tower, filtering photodissociation device, blower fan and aiutage, the filtering photodissociation device include shell, and the shell both ends are set respectively
There are the second air inlet and the second gas outlet, primarily efficient filter layer and photodissociation layer are provided with the shell；The primarily efficient filter layer is close
Second air inlet, including housing, the housing are provided with nonwoven layer, nylon wire, activated carbon filter material, metal hole pattern.
5. purification integrated system according to claim 4, it is characterised in that the housing is paper frame, aluminium frame, galvanized iron
Frame.
6. purification integrated system according to claim 4, it is characterised in that the photodissociation layer includes UV ultraviolet lamps, institute
State and be provided with active nano titanium oxide layer between UV ultraviolet lamps.
7. purification integrated system according to claim 4, it is characterised in that the blower fan is connected to second outlet
Mouthful, it is connected with the aiutage, the high 20m of aiutage on the blower fan.
8. purification integrated system according to claim 4, it is characterised in that the eddy flow tower includes casing, water pump, described
At least two second showers are connected with water pump, second shower is located in the shell；The outer casing bottom is provided with
Eddy flow motor, some swirl vanes are connected with the eddy flow motor.
9. purification integrated system according to claim 8, it is characterised in that the tapered setting of swirl vane, and bore
Shape bottom is provided with blind plate, and the swirl vane edge is provided with guiding gutter, water conservancy diversion is provided between the guiding gutter of adjacent swirl vane
Pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720942709.2U CN207076344U (en) | 2017-07-31 | 2017-07-31 | One kind purification equipment integrating and purification integrated system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720942709.2U CN207076344U (en) | 2017-07-31 | 2017-07-31 | One kind purification equipment integrating and purification integrated system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207076344U true CN207076344U (en) | 2018-03-09 |
Family
ID=61424560
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720942709.2U Expired - Fee Related CN207076344U (en) | 2017-07-31 | 2017-07-31 | One kind purification equipment integrating and purification integrated system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207076344U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261828A (en) * | 2017-07-31 | 2017-10-20 | 苏州绿蓝环保服务有限公司 | One kind purification equipment integrating and purification integrated system |
| CN110280100A (en) * | 2019-06-28 | 2019-09-27 | 深圳市永盛旺机械设备有限公司 | A kind of exhaust gas automatic processing process suitable for spray booth |
-
2017
- 2017-07-31 CN CN201720942709.2U patent/CN207076344U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261828A (en) * | 2017-07-31 | 2017-10-20 | 苏州绿蓝环保服务有限公司 | One kind purification equipment integrating and purification integrated system |
| CN110280100A (en) * | 2019-06-28 | 2019-09-27 | 深圳市永盛旺机械设备有限公司 | A kind of exhaust gas automatic processing process suitable for spray booth |
| CN110280100B (en) * | 2019-06-28 | 2021-10-26 | 深圳市永盛旺机械设备有限公司 | Automatic waste gas treatment process suitable for spraying chamber |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180309 Termination date: 20210731 |