CN205199239U - Little electric charge water sprays handles exhaust unit - Google Patents
Little electric charge water sprays handles exhaust unit Download PDFInfo
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- CN205199239U CN205199239U CN201521052732.1U CN201521052732U CN205199239U CN 205199239 U CN205199239 U CN 205199239U CN 201521052732 U CN201521052732 U CN 201521052732U CN 205199239 U CN205199239 U CN 205199239U
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Abstract
The utility model relates to a little electric charge water sprays handles exhaust unit, including the reaction tower body, wherein the reaction tower internally is equipped with equal air chamber, little electric charge reaction clean room in proper order, sprays the little electric charge reacting chamber of equal hydroecium, water gas separat room and water storage, is equipped with the conductor twine layer that produces little electric charge field in little electric charge reaction clean room, and conductor twine layer top is equipped with the shower, and conductor twine layer electricity is connected with little charge control ware, and beneficial effect is: waste gas get into little electric charge field form take the waste gas and adhesion liquid of polarity particle on, the waste gas of effective interception, capture zone polarity particle, meanwhile can be by flowing of liquid and take away, effective weak point such as the mode of spraying of solving.
Description
Technical field
The utility model relates to a kind of Water spray process waste gas method, specifically a kind of micro-electric charge Water spray process exhaust device.
Background technology
In Water spray process waste gas treatment process, usually utilize the liquid phase of Water spray contrary with the vapor phase movement direction of waste gas, the water-bath liquid phases such as the particulate matter of gas phase, volatile materials, dissolved organic matter are exchanged, liquid phase adsorption takes away purifying exhaust air, flushed in liquid phase granulin molecule substrate tackles pollutant by also adding the fillers such as many water chestnuts shell, ball, net, silk in the process of water adhesion, absorption, improve purification efficiency, during absorption dissolved contaminants, liquid phase is easily satisfied and reduces purification efficiency; In its process, the material of solubility dissolves in water body, and insoluble volatile organic compounds cannot be water-soluble and cannot process.
Summary of the invention
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art, provide a kind of micro-electric charge Water spray process exhaust device, main purpose mainly solves the insoluble volatile organic compounds of spray mode cannot water-soluble problem, and waste water and gas processes simultaneously, plays environmental protection and saving water resource.
One micro-electric charge Water spray process exhaust device that the utility model describes, comprise reaction tower body, wherein be provided with equal air chamber, micro-charge reaction clean room successively in reaction tower body, spray the micro-charge reaction room of equal hydroecium, Ye Qi separation chamber and water storage, the conductor twine layer producing micro-charge field is provided with in micro-charge reaction clean room, be provided with shower above conductor twine layer, conductor twine layer is electrically connected with micro-Charge controlled device.
Further concrete, described conductor twine layer is divided into conductor positive pole conductor twine layer and conductor cathode conductor twine layer, and conductor positive pole conductor twine layer is positioned at above or below conductor cathode conductor twine layer to be located.
Further concrete, described shower is divided into the first shower and the second shower, and the first shower is positioned at above or below the second shower.
Further concrete, described reaction tower body outside is provided with circulation hydroecium, and circulation hydroecium is connected with the micro-charge reaction room of water storage.
Further concrete, described recirculated water indoor are provided with water circulating pump, and the delivery port of water circulating pump is connected with shower.
Further concrete, described reaction tower body sidewall is provided with air inlet, and air inlet is connected with equal air chamber, and reaction tower body top end is provided with gas outlet, and gas outlet is connected with Ye Qi separation chamber.
Further concrete, described water storage micro-charge reaction indoor are provided with micro-charge reaction terminal.
Further concrete, described micro-charge reaction terminal is divided into first micro-charge reaction terminal and second micro-charge reaction terminal, and first micro-charge reaction terminal and second micro-charge reaction terminal are electrically connected with micro-Charge controlled device respectively.
Further concrete, described gas outlet is connected with photocatalyst.
Further concrete, the outlet air end of described photocatalyst is also provided with air-introduced machine.
The beneficial effects of the utility model are: 1, waste gas enters micro-charge field and forms the waste gas of band polar particle and the waste gas on adhering liquid, effectively tackling, catch band polar particle; Meanwhile pollute and taken away by the flowing of liquid, further purifying exhaust air, effectively solving the insoluble volatile organic compounds of spray mode cannot water-soluble problem; 2, during process, sewage is constantly oxidized in the micro-charge reaction room of water storage and purifies, the outer row of circulating and recovering, plays waste gas, waste water and processes simultaneously and do not produce secondary pollution, play saving water resource.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the first using state structural representation of the present invention.
Fig. 3 is the second using state structural representation of the present invention.
The icon of the following drawings illustrates:
Reaction tower body 1; Air inlet 2; Equal air chamber 3; Micro-charge reaction clean room 4; Conductor positive pole conductor twine layer 41; Conductor cathode conductor twine layer 42; First shower 45; Spray equal hydroecium 5; Second shower 51; Ye Qi separation chamber 6; Gas outlet 7; The micro-charge reaction room 8 of water storage; First micro-charge reaction terminal 81; Second micro-charge reaction terminal 82; Circulation hydroecium 9; Water circulating pump 10; Micro-Charge controlled device 11.
Detailed description of the invention
Below by accompanying drawing, embodiment of the present utility model is further illustrated.
Describe according to the one of the utility model embodiment micro-electric charge Water spray process exhaust device below with reference to Fig. 1 to Fig. 3.
As shown in Figure 1 to Figure 3, one micro-electric charge Water spray process exhaust device that the utility model describes, comprise reaction tower body 1, wherein be provided with equal air chamber 3, micro-charge reaction clean room 4 successively in reaction tower body 1, spray the micro-charge reaction room 8 of equal hydroecium 5, Ye Qi separation chamber 6 and water storage, the conductor twine layer producing micro-charge field is provided with in micro-charge reaction clean room 4, be provided with shower above conductor twine layer, conductor twine layer is electrically connected with micro-Charge controlled device 11.
Further concrete, described conductor twine layer is divided into conductor positive pole conductor twine layer 41 and conductor cathode conductor twine layer 42, and conductor positive pole conductor twine layer 41 is positioned at above or below conductor cathode conductor twine layer 42 to be located.Described shower is divided into the first shower 45 and the second shower 51, first shower 45 to be positioned at above or below the second shower 51.
Further concrete, described reaction tower body 1 outside is provided with circulation hydroecium 9, and circulation hydroecium 9 is connected with the micro-charge reaction room 8 of water storage.
Further concrete, be provided with water circulating pump 10 in described circulation hydroecium 9, the delivery port of water circulating pump 10 is connected with shower.
Further concrete, described reaction tower body 1 sidewall is provided with air inlet 2, and air inlet 2 is connected with equal air chamber 3, and reaction tower body 1 top end is provided with gas outlet 7, and gas outlet 7 is connected with Ye Qi separation chamber 6.
Further concrete, micro-charge reaction terminal is provided with in described water storage micro-charge reaction room 8, described micro-charge reaction terminal is divided into first micro-charge reaction terminal 81 and the micro-charge reaction terminal of second micro-charge reaction terminal 82, first 81 and second micro-charge reaction terminal 82 to be electrically connected with micro-Charge controlled device 11 respectively.
Further concrete, described gas outlet 7 place is connected with photocatalyst.The outlet air end of described photocatalyst is also provided with air-introduced machine.
As shown in Figure 1 to Figure 3, this method is provided with waste gas and enters in micro-charge reaction clean room 4 through air inlet 2 by equal air chamber 3, enter levels separation in micro-charge reaction clean room and the vapor phase contaminants acquisition polarity charge that conductor positive pole conductor twine layer 41 adheres to liquid phase is set, enter the contrary conductor cathode conductor twine layer 42 upper strata charge field absorption interception of polarity charge, catch liquid phase adhered particles, gas phase after waste gas purification enters Ye Qi separation chamber 6 by the equal hydroecium 5 of spray and is discharged by gas outlet, top 7, forms gas phase purifying path; The liquid that first shower 45, second shower 51 is carried and the dye thing taken away enter the micro-charge reaction room 8 of water storage and carry out advanced oxidation reaction purification, circulation hydroecium 9 is entered by bottom the micro-charge reaction room 8 of water storage, be transported to the first shower 45 and the second shower 51 by water circulating pump 10 and enter the equal hydroecium 5 of spray and micro-charge reaction clean room 4, such circulation forms liquid phase water loop; Micro-Charge controlled device 11 controls to be transported to by the different power supply way of outputs on conductor cathode conductor twine layer 42 in micro-charge reaction clean room 4, conductor positive pole conductor twine layer 41, in addition, the micro-charge reaction terminal 82 of first micro-charge reaction terminal 81, second carrying electricity to water storage micro-charge reaction room 8 is with positive and negative electric charge to form electric loop respectively, and conveying power supply works to water circulating pump 10 and forms circulating water loop;
Therefore, the sewage treatment step of blanket the utility model: step one: waste gas to be entered in micro-charge reaction clean room by equal air chamber through air inlet and carries out purified treatment; Step 2: waste gas is entered micro-charge reaction clean room through reaction tower body bottom air inlet by equal air chamber and discharged by gas outlet, top, Ye Qi separation chamber by the equal hydroecium of spray, forms gas phase purifying path; Step 3: in micro-charge reaction clean room, levels is separated and arranged conductor twine layer and connect external power by conducting terminal, consists of the electric loop of conductor positive pole twine layer and conductor negative pole twine layer respectively; Step 4: the adhesion of liquid phase mass transfer exchange pollutant is depended on liquid phase and entered the micro-charge field polarity conductor twine layer of band, motion absorption electric charge is formed as being with polar particle from bottom to top, enter opposite polarity conductor twine micro-charge field layer absorption interception, catch, gas phase purifying is arranged outward, and liquid phase takes away vapor phase contaminants; Step 5: water storage micro-charge reaction room enters water circulating pump through circulation hydroecium and is transported to the equal hydroecium of spray, forms the liquid-phase loop constantly circulating, constantly purify; Liquid phase makes circular treatment by above-mentioned steps one to five, and the liquid phase fluid direction of motion is contrary with the direction of motion of gaseous fluid, and the water in processing procedure is without the need to discharging discharge.
Waste gas enters micro-charge reaction clean room 4 through reaction tower body 1 bottom air inlet 2 by equal air chamber 3 and enters the equal hydroecium 5 of spray and discharged by gas outlet, top, Ye Qi separation chamber 67.Liquid phase liquid enters circulation hydroecium 9 by bottom the micro-charge reaction room 8 of water storage, is transported to the first shower 45, second shower 51 and enters the equal hydroecium 5 of spray and micro-charge reaction clean room 4, form liquid phase water closed circuit by water circulating pump 10.
As shown in Figure 2, described micro-Charge controlled device 11 controls to be transported to micro-charge reaction clean room 4 electric charge by the different power supply way of outputs and forms electric loop, carry electricity to water storage micro-charge reaction room 8 and form electric loop, conveying power supply is to water circulating pump 10, reaction tower body 1 is insulating materials, equal air chamber 3 unit is provided with operation window 12, and micro-charge reaction clean room 4 unit is provided with operation window 121, sprays equal hydroecium 5 unit and is provided with operation window 122.
This micro-Charge controlled device 11 carries power supply to form electric loop to the terminal of the conductor positive pole conductor twine layer 41 of micro-charge reaction clean room 4, conductor cathode conductor twine layer 42 as shown in Figure 3, terminal and conductor twine connected mode, directly naturally stacked with the strip conductor of band terminal by twine to contact or prick that bind is tactile connects, conductor cathode conductor twine layer 42 is by the first insulation grid 43 support, and conductor positive pole conductor twine layer 41 is by the second insulation grid 43 support; Micro-Charge controlled device 11 carries power supply to form electric loop to the micro-charge reaction terminal 82 of first micro-charge reaction terminal 81, second of water storage micro-charge reaction room 8.
The conductor cathode conductor twine layer 42 of micro-charge reaction clean room 4 of micro-electric charge Water spray process waste gas, the terminal of conductor positive pole conductor twine layer 41 form electric loop, can arrange 1 group, 2 groups and many group homogeneous structures micro-conductor twine electricity circuit units in reaction tower body 1.
On be only preferred embodiment of the present utility model, not in order to limit the utility model, all do within spirit of the present utility model and principle any amendment, equivalent to replace or improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. a micro-electric charge Water spray process exhaust device, comprise reaction tower body (1), it is characterized in that: be provided with equal air chamber (3), micro-charge reaction clean room (4) successively in reaction tower body (1), spray equal hydroecium (5), Ye Qi separation chamber (6) and the micro-charge reaction room (8) of water storage, the conductor twine layer producing micro-charge field is provided with in micro-charge reaction clean room (4), be provided with shower above conductor twine layer, conductor twine layer is electrically connected with micro-Charge controlled device (11).
2. one according to claim 1 micro-electric charge Water spray process exhaust device, it is characterized in that: described conductor twine layer is divided into conductor positive pole conductor twine layer (41) and conductor cathode conductor twine layer (42), conductor positive pole conductor twine layer (41) is positioned at above or below conductor cathode conductor twine layer (42) to be located.
3. one according to claim 1 micro-electric charge Water spray process exhaust device, it is characterized in that: described shower is divided into the first shower (45) and the second shower (51), and the first shower (45) is positioned at above or below the second shower (51).
4. one according to claim 1 micro-electric charge Water spray process exhaust device, is characterized in that: described reaction tower body (1) outside is provided with circulation hydroecium (9), and circulation hydroecium (9) is connected with the micro-charge reaction room (8) of water storage.
5. one according to claim 4 micro-electric charge Water spray process exhaust device, is characterized in that: be provided with water circulating pump (10) in described circulation hydroecium (9), the delivery port of water circulating pump (10) is connected with shower.
6. one according to claim 1 micro-electric charge Water spray process exhaust device, it is characterized in that: described reaction tower body (1) sidewall is provided with air inlet (2), air inlet (2) is connected with equal air chamber (3), reaction tower body (1) top end is provided with gas outlet (7), and gas outlet (7) are connected with Ye Qi separation chamber (6).
7. one according to claim 1 micro-electric charge Water spray process exhaust device, is characterized in that: be provided with micro-charge reaction terminal in described water storage micro-charge reaction room (8).
8. one according to claim 7 micro-electric charge Water spray process exhaust device, it is characterized in that: described micro-charge reaction terminal is divided into first micro-charge reaction terminal (81) and second micro-charge reaction terminal (82), first micro-charge reaction terminal (81) and second micro-charge reaction terminal (82) are electrically connected with micro-Charge controlled device (11) respectively.
9. one according to claim 6 micro-electric charge Water spray process exhaust device, is characterized in that: described gas outlet (7) place is connected with photocatalyst.
10. one according to claim 9 micro-electric charge Water spray process exhaust device, is characterized in that: the outlet air end of described photocatalyst is also provided with air-introduced machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521052732.1U CN205199239U (en) | 2015-12-17 | 2015-12-17 | Little electric charge water sprays handles exhaust unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521052732.1U CN205199239U (en) | 2015-12-17 | 2015-12-17 | Little electric charge water sprays handles exhaust unit |
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| CN205199239U true CN205199239U (en) | 2016-05-04 |
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| CN201521052732.1U Active CN205199239U (en) | 2015-12-17 | 2015-12-17 | Little electric charge water sprays handles exhaust unit |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111036070A (en) * | 2020-01-06 | 2020-04-21 | 哈尔滨工业大学 | Polarity bionic aquatic weed enhanced ecological indoor air purification device and method |
-
2015
- 2015-12-17 CN CN201521052732.1U patent/CN205199239U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111036070A (en) * | 2020-01-06 | 2020-04-21 | 哈尔滨工业大学 | Polarity bionic aquatic weed enhanced ecological indoor air purification device and method |
| CN111036070B (en) * | 2020-01-06 | 2021-11-30 | 哈尔滨工业大学 | Polarity bionic aquatic weed enhanced ecological indoor air purification device and method |
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