CN205216575U - High pressure spraying exhaust treatment device - Google Patents
High pressure spraying exhaust treatment device Download PDFInfo
- Publication number
- CN205216575U CN205216575U CN201521002973.5U CN201521002973U CN205216575U CN 205216575 U CN205216575 U CN 205216575U CN 201521002973 U CN201521002973 U CN 201521002973U CN 205216575 U CN205216575 U CN 205216575U
- Authority
- CN
- China
- Prior art keywords
- pressure pump
- pressure
- control equipment
- valve
- dispensing box
- 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
Abstract
The utility model relates to an exhaust treatment device especially relates to the high pressure spraying exhaust treatment device pollution -free, that the treatment effect is good. Including pure water case, concentrate tank, liquid preparation box, high -pressure pump, ball valve and atomizer, pure water case and concentrate tank be connected with liquid preparation box respectively, liquid preparation box pass through the high -pressure pump and be connected with the atomizer, the high -pressure pump connect four atomizers through four mist spraying pipeline of group respectively, wherein be provided with on two sets of mist spraying pipeline and be provided with ball valve and solenoid valve on ball valve, the other two sets of mist spraying pipeline. The utility model discloses utilize the nanometer microbubble to handle the VOC in the waste gas and utilize the biological enzyme to eliminate waste gas.
Description
[technical field]
The utility model relates to a kind of emission-control equipment, especially relates to a kind of pollution-free, the high-pressure fog emission-control equipment that treatment effect is good.
[background technology]
VOC material refers to the general name holding volatile organic substance at normal temperatures, common are formaldehyde, toluene and dimethylbenzene etc.Traditional spraying industry uses a large amount of nitrate paint raw and auxiliary materials in goods spraying process, nitrate paint raw and auxiliary material contains a large amount of machine solvents, especially the aromatic hydrocarbon that contains of the high volatile solvent such as dimethylbenzene, toluene, benzene is not only poisonous but also inflammable, and highly volatile is in environment, cause and discharged numerous VOC in air, pollutant atmosphere and being detrimental to health.In the process of industrial waste gas, major part adopts chemicals to carry out chemical reaction for corresponding waste gas, to realize the object of exhaust-gas treatment.But this processing mode not only cost is high, process is thorough not, and has the danger of secondary pollution.In order to solve the problem, there is the method for the physical characteristic process industrial waste gas utilizing nano bubble, the use of mixed biologic enzyme, both can eliminate the chemical residual in industrial waste gas, and can peculiar smell have been removed again, and there is no the danger of secondary pollution.But when utilizing biology enzyme mixed liquor, often there is waste, improve the cost of business processes waste gas.But there is water miscible biology enzyme when mixing with water by Artificial Control matched proportion density not only waste of manpower resource, also matched proportion density can be caused to differ due to reasons such as operate misses simultaneously, affect production efficiency.
[summary of the invention]
The utility model is intended to solve the problem and provides a kind of emission-control equipment utilizing the VOC in nanoscale microbubble process waste gas and utilize biology enzyme elimination peculiar smell.
For achieving the above object, a kind of high-pressure fog emission-control equipment of the present utility model, comprise pure water tank 10, stoste case 20, dispensing box 50, high-pressure pump 60, ball valve 70 and atomizer 100, described pure water tank 10 is connected with dispensing box 50 respectively with stoste case 20, described dispensing box 50 is connected with atomizer 100 by high-pressure pump 60, described high-pressure pump 60 connects four atomizers 100 respectively by four groups of spray pipes, wherein two groups of spray pipes is provided with on ball valve 70, other two groups of spray pipes and is provided with ball valve 70 and magnetic valve 80.
Further, described magnetic valve 80 is arranged between ball valve 70 and atomizer 100.
Further, be also connected with waste water reclaiming device 90, waste water reclaiming device is connected to exhaust piping wall bottom position.
Further, described stoste case 20 inner upper is provided with high water level checkout gear 21, and stoste case 20 lower inside is provided with low water level checkout gear 22, and the water-head between high water level checkout gear 21 and low water level checkout gear 22 is fixed value.
Further, described pure water tank 10 inner upper is provided with automatic water compensating valve 11, and automatic water compensating valve 11 controls the most high liquid level (HLL) of pure water tank 10.
Further, described pure water tank 10 connects dispensing box 50 by circulating pump 40, and described stoste case 20 is connected with dispensing box 50 by measuring pump 30.
Further, described dispensing box 50 is also connected with mixing pump 51, and the entrance of described mixing pump 51 is all connected on dispensing box 50 with outlet.
Further, described high-pressure pump 60 is also parallel with secondary high-pressure pump 61, and described high-pressure pump 60 takes turns to operate with secondary high-pressure pump 61.
Further, described high-pressure pump 60, secondary high-pressure pump 61 export and are also parallel with relief valve 63 and return valve 62, and described relief valve 63 is connected dispensing box 50 with the outlet of return valve 62.
Contribution of the present utility model there are provided a kind of emission-control equipment utilizing the VOC in nanoscale microbubble process waste gas and utilize biology enzyme elimination peculiar smell.This device produces nanoscale bubble by atomizer, nanoscale bubble explosion thus decompose containing the organic compound molecule in the gas of VOC, can not to environment, also do not need to use any oxidant, whole decomposable processes only needs water to participate in; And the water after reclaiming in circulating water device, can participate in the processing procedure containing VOC gas through steps such as filtrations again, there is no any loss; Owing to there is no the participation of other oxidants, except environment and human body are not affected, also alleviate the processing load of discharger greatly.This device is provided with four groups of spray pipes, wherein two groups directly spray, other two group pulse sprayings, pulse nebulization technique can freely close and open under the work of magnetic valve, spraying is controlled effectively at any time, when waste gas peculiar smell is little, the consumption of biology enzyme can be reduced, for enterprise reduces production cost as far as possible.And this device can control matched proportion density automatically, easy to use, liberate a large amount of human resources, and the exhaust-gas treatment cost of enterprise can not have been increased because of human error.
[accompanying drawing explanation]
Fig. 1 is structural representation of the present utility model.
[detailed description of the invention]
The following example is to further explanation of the present utility model and supplements, and does not constitute any limitation the utility model.
Embodiment 1
As shown in Figure 1, a kind of high-pressure fog emission-control equipment of the present embodiment comprises: pure water tank 10, stoste case 20, dispensing box 50, high-pressure pump 60, ball valve 70 and atomizer 100, described pure water tank 10 is connected with dispensing box 50 respectively with stoste case 20, described dispensing box 50 is connected with atomizer 100 by high-pressure pump 60, described high-pressure pump 60 connects four atomizers 100 respectively by four groups of spray pipes, wherein two groups of spray pipes is provided with on ball valve 70, other two groups of spray pipes and is provided with ball valve 70 and magnetic valve 80.The water being atomized out via atomizer 100 can form nano level bubble, and the collapse of nanometer bubble can produce ultrasonic wave and extrude fluid molecule, changes the density that medium is original, makes it increase; And when sparse phase place, make fluid molecule sparse, discrete further, the density of medium reduces.When with the ul-trasonic irradiation of enough large amplitudes in liquid medium time, in negative pressure phase (i.e. sparse phase), average departure defection between fluid molecule exceedes the scf molecule distance that liquid medium is remained unchanged, liquid medium will rupture, form microvesicle, microvesicle grows up into cavitation bubble further.These bubbles can be dissolved among liquid medium on the one hand again, also may float and disappear; On the other hand, continue to grow up along with the change of sound field, until negative pressure reaches maximum, in back to back compression process, these cavitation bubbles are compressed, and its bodily form reduces, and what have even affects the organic factor of ultrasonic degradation.Secondly, when liquid is in ultrasonic field, pressure wave forms condition of high voltage, is enough to open the stronger chemical bond of adhesion, makes hydrone H
2o is decomposed into-H and-OH free radical or generates H
2o
2, the oxidative free radical of generation is diffused in water body, then is reacted by the mode of nanometer bubble and VOC.Again, nanoscale bubble, in the moment of collapse, produces the high temperature of 4000K.This extreme environment enters the organic gas of nanoscale bubble to volatilization, and the organic matter at nanoscale bubble gas-liquid interface place, has the effect of pyrolysis scission of link, VOC is degraded.The diameter of nanoscale bubble that this device produces is 50-500 nanometer, means that the water of equal quality can produce more nanoscale bubble, can more fully with the gas and vapor permeation containing VOC, degrade more thorough.Water in dispensing box 50 resolves into nano level bubble by atomizer 100, bubble with containing VOC gas and vapor permeation thus VOC is decomposed, biology enzyme in dispensing box 50 then produces chemical reaction with the odor molecules in waste gas, that odor molecules is degraded, thus the peculiar smell in elimination waste gas, reach the object of exhaust-gas treatment.
Embodiment 2
As shown in Figure 1, described magnetic valve 80 is arranged between ball valve 70 and atomizer 100.In the present embodiment, high-pressure pump 60 is connected with 4 atomizers 100, wherein two atomizers 100 connect ball valve 70, and two other atomizer 100 connects ball valve 70 and magnetic valve 80, and magnetic valve 80 can open and close under control, thus control the opening and closing of atomizer 100, if the peculiar smell of waste gas is also not obvious, the quantity of the atomizer 100 used can be reduced, therefore magnetic valve 80 can cut out, if the peculiar smell of waste gas is obvious, magnetic valve 80 can be opened.
Embodiment 3
As shown in Figure 1, a kind of high-pressure fog emission-control equipment of the present embodiment is also connected with waste water reclaiming device 90, and waste water reclaiming device is connected to exhaust piping wall bottom position.Finally still form water after the explosion of nanoscale bubble, reclaim if the water in exhaust piping is not discharged, can line clogging be made, affect the speed of exhaust-gas treatment.
Embodiment 4
As shown in Figure 1, in the present embodiment, described stoste case 20 inner upper is provided with high water level checkout gear 21, and stoste case 20 lower inside is provided with low water level checkout gear 22, and the water-head between high water level checkout gear 21 and low water level checkout gear 22 is fixed value.Can ensure that the storage of biology enzyme in stoste case 20 is in fixed range like this, described pure water tank 10 connects dispensing box 50 by circulating pump 40, and described stoste case 20 is connected with dispensing box 50 by measuring pump 30.Because the price of biology enzyme own is high, so need the ratio of biology enzyme to be reduced when biology enzyme and water being mixed as far as possible, thus reduce the exhaust-gas treatment cost of enterprise, therefore, the use of measuring pump 30 just can ensure that the amount of the biology enzyme at every turn entered in dispensing box 50 is fixed
Embodiment 5
As shown in Figure 1, described pure water tank 10 inner upper is provided with automatic water compensating valve 11, and automatic water compensating valve 11 controls the most high liquid level (HLL) of pure water tank 10.Because needs mix biology enzyme and water, therefore, the control of ratio just becomes a problem that must solve, in the present embodiment, the amount of the water at every turn mixed is fixed, so just can by only adjusting the amount of biology enzyme, thus realize the mixing of fixed proportion, automatic water compensating valve 11 controls the most high liquid level (HLL) of pure water tank 10, when the water in each pure water tank 10 reaches automatic water compensating valve 11 position, stops supplying water in pure water tank 10.
Embodiment 6
As shown in Figure 1, the dispensing box 50 of the present embodiment is also connected with mixing pump 51, and the entrance of described mixing pump 51 is all connected on dispensing box 50 with outlet.This kind of design can make water and biology enzyme mixing more fully, avoids ratio uneven.
Embodiment 7
In the present embodiment, high-pressure pump 60 is also parallel with secondary high-pressure pump 61, and described high-pressure pump 60 takes turns to operate with secondary high-pressure pump 61.General setting high-pressure pump 60 stops after working 10 hours, and secondary high-pressure pump 61 is started working, and then secondary high-pressure pump 61 stops after working 5 hours, and high-pressure pump 60 is started working.Take turns to operate and can extend the service life of high-pressure pump 60 and secondary high-pressure pump 61.
Embodiment 8
As shown in Figure 1, described high-pressure pump 60, secondary high-pressure pump 61 export and are also parallel with relief valve 63 and return valve 62, and described relief valve 63 is connected dispensing box 50 with the outlet of return valve 62.In order to reduce the waste of biology enzyme, the present embodiment exports also be parallel with relief valve 63 and return valve 62 at described high-pressure pump 60, secondary high-pressure pump 61, and described relief valve 63 is connected dispensing box 50 with the outlet of return valve 62.When magnetic valve 80 cuts out, pressure in pipeline raises, relief valve 63 works, manifold pressure is returned and drops to point of safes, if force value is too high, spray velocity being made to accelerate thus cause biology enzyme consumption excessive, connecting return valve 62 for avoiding this situation in high-pressure pump 60, secondary high-pressure pump 61 exit, return valve 62 outlet is connected to dispensing box 50, realizes the recovery of biology enzyme.
Although disclosed the utility model by above embodiment; but protection domain of the present utility model is not limited thereto; under the condition not departing from the utility model design, all will fall in right of the present utility model the distortion, replacement etc. that above each component does.
Claims (9)
1. a high-pressure fog emission-control equipment, comprise pure water tank (10), stoste case (20), dispensing box (50), high-pressure pump (60), ball valve (70) and atomizer (100), described pure water tank (10) is connected with dispensing box (50) respectively with stoste case (20), described dispensing box (50) is connected with atomizer (100) by high-pressure pump (60), it is characterized in that: described high-pressure pump (60) connects four atomizers (100) respectively by four groups of spray pipes, wherein two groups of spray pipes are provided with ball valve (70), other two groups of spray pipes are provided with ball valve (70) and magnetic valve (80).
2. a kind of high-pressure fog emission-control equipment as claimed in claim 1, is characterized in that: described magnetic valve (80) is arranged between ball valve (70) and atomizer (100).
3. a kind of high-pressure fog emission-control equipment as claimed in claim 2, it is characterized in that: be also connected with waste water reclaiming device (90), waste water reclaiming device is connected to exhaust piping wall bottom position.
4. a kind of high-pressure fog emission-control equipment as described in as arbitrary in claim 1-3, it is characterized in that: described stoste case (20) inner upper is provided with high water level checkout gear (21), stoste case (20) lower inside is provided with low water level checkout gear (22), and the water-head between high water level checkout gear (21) and low water level checkout gear (22) is fixed value.
5. a kind of high-pressure fog emission-control equipment as claimed in claim 4, it is characterized in that: described pure water tank (10) inner upper is provided with automatic water compensating valve (11), automatic water compensating valve (11) controls the most high liquid level (HLL) of pure water tank (10).
6. a kind of high-pressure fog emission-control equipment as claimed in claim 5, it is characterized in that: described pure water tank (10) connects dispensing box (50) by circulating pump (40), and described stoste case (20) is connected with dispensing box (50) by measuring pump (30).
7. a kind of high-pressure fog emission-control equipment as claimed in claim 6, it is characterized in that: described dispensing box (50) is also connected with mixing pump (51), the entrance of described mixing pump (51) is all connected on dispensing box (50) with outlet.
8. a kind of high-pressure fog emission-control equipment as claimed in claim 7, it is characterized in that: described high-pressure pump (60) is also parallel with secondary high-pressure pump (61), described high-pressure pump (60) and secondary high-pressure pump (61) take turns to operate.
9. a kind of high-pressure fog emission-control equipment as claimed in claim 8, it is characterized in that: the outlet of described high-pressure pump (60), secondary high-pressure pump (61) is also parallel with relief valve (63) and return valve (62), and described relief valve (63) is connected dispensing box (50) with the outlet of return valve (62).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002973.5U CN205216575U (en) | 2015-12-04 | 2015-12-04 | High pressure spraying exhaust treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521002973.5U CN205216575U (en) | 2015-12-04 | 2015-12-04 | High pressure spraying exhaust treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205216575U true CN205216575U (en) | 2016-05-11 |
Family
ID=55891671
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521002973.5U Active CN205216575U (en) | 2015-12-04 | 2015-12-04 | High pressure spraying exhaust treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205216575U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109316924A (en) * | 2017-12-14 | 2019-02-12 | 深圳市科延机电有限公司 | A kind of smoke multistage purification device, purification method and smokeless reflow machine |
| CN114931853A (en) * | 2022-07-26 | 2022-08-23 | 苏州博纽强新材料科技有限公司 | Trapping CO in cement kiln flue gas 2 Method for synergistically preparing low-carbon cement and obtained product |
-
2015
- 2015-12-04 CN CN201521002973.5U patent/CN205216575U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109316924A (en) * | 2017-12-14 | 2019-02-12 | 深圳市科延机电有限公司 | A kind of smoke multistage purification device, purification method and smokeless reflow machine |
| CN114931853A (en) * | 2022-07-26 | 2022-08-23 | 苏州博纽强新材料科技有限公司 | Trapping CO in cement kiln flue gas 2 Method for synergistically preparing low-carbon cement and obtained product |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108004847B (en) | Ancient book deacidification and restoration method | |
| CN205216575U (en) | High pressure spraying exhaust treatment device | |
| CN204237602U (en) | A kind of energy-conservation comprehensive chemical industry advanced waste treatment system | |
| CN205109392U (en) | Absorption process and biological method combined effect handle device of VOC waste gas | |
| CN201171809Y (en) | Biology deodorization reaction device | |
| CN107261183A (en) | Spray deodorizer | |
| CN204051465U (en) | A kind of high-concentrated ozone Water generator | |
| CN116173874A (en) | Production equipment of waterborne epoxy resin anticorrosive paint and application method thereof | |
| CN207805577U (en) | A kind of waste oil catalytic cracking reaction equipment | |
| CN211644822U (en) | Industrial sewage filtering device | |
| CN207342443U (en) | A kind of lacquer spraying waste gas integrated treatment unit | |
| CN206375795U (en) | A kind of automated programming system containing organic matter and inorganic salts waste water | |
| CN213493425U (en) | A cyclic utilization device for water based paint production | |
| CN205867955U (en) | Waste gas treatment system between spraying shop, levelling room, accent lacquer | |
| CN208177244U (en) | A kind of biology removes the water-soluble absorption plant of benzene class and its derivative | |
| CN207756370U (en) | A kind of environmentally friendly automatic paint-spraying machine | |
| CN202277551U (en) | Spray deodorization system of garbage transfer station | |
| CN209317419U (en) | A kind of device of vehicle repairing factory exhaust gas waste water collaboration processing | |
| CN206168070U (en) | Leachate treatment system | |
| CN205599373U (en) | Mucilage binding that spouts that two ingredients were glued is put | |
| CN201316701Y (en) | Paint flow control device | |
| CN212152026U (en) | Device for repairing heavy metal sludge | |
| CN205216576U (en) | High pressure water -spraying system | |
| CN204550136U (en) | Galley oil and water treatment equipment | |
| CN209259816U (en) | A kind of coating material production wastewater treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |