CN203360086U - Ozone gas-liquid exchange device and water purification and disinfection device applying same - Google Patents
Ozone gas-liquid exchange device and water purification and disinfection device applying same Download PDFInfo
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- CN203360086U CN203360086U CN 201320411844 CN201320411844U CN203360086U CN 203360086 U CN203360086 U CN 203360086U CN 201320411844 CN201320411844 CN 201320411844 CN 201320411844 U CN201320411844 U CN 201320411844U CN 203360086 U CN203360086 U CN 203360086U
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Abstract
The utility model discloses an ozone gas-liquid exchange device and a water purification and disinfection device applying the ozone gas-liquid exchange device. The ozone gas-liquid exchange device is characterized in that an upright umbrella rotation gas-liquid transfer device driven by a driving motor is matched with an ozone bubbling aerator, or an inverted umbrella rotation gas-liquid transfer device driven by the driving motor is matched with a flow guide lifting barrel and the ozone bubbling aerator. The gas-liquid mass transfer efficiency of the ozone gas-liquid exchange device is high. The water purification and disinfection device applying the ozone gas-liquid exchange device comprises an ozone generator unit, an ozone tail gas removal unit and the ozone gas-liquid exchange device, and can further comprise an active carbon filter device which is arranged at the front end and/or the rear end of the ozone gas-liquid exchange device and communicated with the ozone gas-liquid exchange device. The water purification and disinfection device is high in efficiency, low in cost and good in safety, and can be used for purifying and disinfecting fish culture sewage, recreational water, domestic water and drinking water.
Description
Technical field
The utility model relates to a kind of ozone gas-liquid exchange device and applies its water purifying and sterilizing device.
Background technology
China is that world population density is the highest, Economic development is the soonest, also one of the most serious country of environmental pollution, and water is Source of life, and it is invisible killer that various water pollutes, and causes relative disease sickness rate rapid development.
Ozone is one of the most effective cold sterilization material, can kill bacteria and virus, eliminate agricultural chemicals and chemical substance, and utilize ozone purification water can remove look, taste removal, and there is no chemical residual.The ozone wide material sources, can obtain by the oxygen that activates occurring in nature.
Utmost point easy bacteria-developing when traditional active carbon purifying is processed water, form bacterial biof iotalm BIOFILM and cause the secondary pollution of water, ozone, in conjunction with the gac water treatment method, can overcome above-mentioned shortcoming, at gac interface formation advanced oxidation, further purifies waste water simultaneously.Ozone gas-liquid mass transfer technology is the applied science technology, and traditional ozone gas-liquid mass transfer method comprises high pressure aeration and high-pressure spray formula.Also do not apply at present ozone gas-liquid transmission method and the device of non-high-pressure spray.
Ozone (air source or source of oxygen) gac water treatment method is applicable to large-scale aquarium water purifying sterilizing, supports the fish tank water purifying sterilizing, rearing pond water purifying sterilizing, life in the countryside water and drink water purifying sterilization, household water and tap water dechlorination purifying sterilizing, city recreational water (water slide, fountain, swimming pool) purifying sterilizing.
The utility model content
First purpose of the present utility model is to provide a kind of ozone gas-liquid exchange device non-high-pressure spray, that gas-liquid mass transfer efficiency is high that adopts.
For achieving the above object, the utility model adopts following technical scheme:
A kind of ozone gas-liquid exchange device, comprise shell, drive-motor, ozone bubbling aerator, described drive-motor is fixed on cover top portion, and described shell surrounds and forms the gas-liquid exchange storehouse that comprises Qi Canghe bottom, top sump, and described ozone bubbling aerator is fixed in sump; Also comprise positive umbellate form rotating gas-liquid transfer device, described positive umbellate form rotating gas-liquid transfer device comprises the umbrella handle axle and is arranged on the positive canopy of umbrella handle axle lower end; Described drive-motor is connected with the upper end of umbrella handle axle, and described positive canopy is positioned at sump, and described ozone bubbling aerator is positioned at the umbrella mouth below of positive canopy; Or also comprise that inversed umbrella type rotating gas-liquid transfer device and water conservancy diversion enhancing tube, described inversed umbrella type rotating gas-liquid transfer device comprise the umbrella handle axle and be arranged on the canopy that falls of umbrella handle axle lower end; Described drive-motor is connected with the upper end of umbrella handle axle, described canopy is positioned at sump, and the described umbrella top of canopy is positioned at the top end opening place of water conservancy diversion enhancing tube, and described water conservancy diversion enhancing tube is fixed in sump, and described ozone bubbling aerator is arranged on the bottom end opening place of water conservancy diversion enhancing tube.
Further, described gas-liquid exchange storehouse is thin and tall type gas-liquid exchange storehouse.
Further, described positive canopy or the canopy of canopy of falling comprise the umbellate form retaining plate, be provided with a plurality of ventilating pits on described umbellate form retaining plate, and the described umbellate form retaining plate outside are installed with laminated plastics or metal hole pattern.
Further, described ozone bubbling aerator is to have a plurality of annular hollow ventpipes that are uniformly distributed eyelet.
Further, described shell top is provided with water inlet, and described water inlet front end is communicated with inhalent siphon, and described inhalent siphon is provided with into water pump and enters electromagnetic valve for water pump; Described shell bottom is provided with water outlet, and described water outlet rear end is communicated with rising pipe, and described rising pipe is provided with out water pump; The intersection of described gas storehouse and sump is provided with the water-level detecting function unit, is arranged on the sidewall of described shell; Described water-level detecting function unit comprises water level float and dry-reed tube magnetic force water level control post, described water level is controlled post and is set to level Four, be that first step water level is that water level is shut down in the warning of water overfill, second stage water level is for bringing into operation and continuing operating water level, third stage water level is for adding water and continuing operating water level, and fourth stage water level is the lack of water water level out of service of reporting to the police; Described ozone gas-liquid exchange device also comprises electric control gear, and described electric control gear is controlled described water-level detecting function unit and entered electromagnetic valve for water pump.
Second purpose of the present utility model is to provide the water purifying and sterilizing device that a kind of efficiency is high, cost is low, security is good that comprises above-mentioned ozone gas-liquid exchange device.
For achieving the above object, the utility model adopts following technical scheme:
A kind of water purifying and sterilizing device, comprise above-mentioned ozone gas-liquid exchange device, also comprises ozonizer unit, ozone tail gas elimination unit; Described ozonizer unit is communicated with ozone bubbling aerator, and ozone tail gas is eliminated Yu Qi storehouse, unit and is communicated with.
Further, a plurality of ozonizer groups that described ozonizer unit comprises the air drying agent post and is communicated with the air drying agent post, described ozonizer group comprises the air pump be communicated with the air drying agent post and the ozonizer be communicated with air pump, described ozonizer inside is provided with radiator fan, described ozonizer is provided with the ozone outlet pipe, and described outlet pipe is provided with cooling gas check valve; Described a plurality of ozonizer group while or alternate run; Described air drying agent post front end is connected with oxygenerator or the air drying agent post is direct and air communication.
Further, described ozone tail gas is eliminated unit and is comprised interconnected ceramic PTC thermal degradation device and charcoal manganese post, and described ceramic PTC thermal degradation device is arranged on the front end of charcoal manganese post.
Further, described ozone gas-liquid exchange device, ozonizer unit, ozone tail gas are eliminated unit and are installed in a main body cover, and at described main body cover inwall, radiator fan also be installed.
Further, also comprise the active carbon filtering device that is arranged on end before or after the ozone gas-liquid exchange device, is communicated with the ozone gas-liquid exchange device.
Further, described active carbon filtering device comprises body fuselage, is arranged on water inlet, water outlet, sewage draining exit and base on body fuselage; Described water inlet front end is provided with into water pump, and the water inlet rear end is communicated with into the water mixing chamber, describedly enters water mixing chamber rear end and is provided with filter cotton A; Described water outlet rear end is provided with and distributes the mouth of a river, and the water outlet front end is communicated with the water outlet mixing chamber, and described water outlet mixing chamber front end is provided with filter cotton B; Between described filter cotton A, B, the activated carbon filtration post is set, is filled in described body fuselage inside.
Further, also comprise the outlet switch and working time control unit, for controlling described active carbon filtering device and ozone gas-liquid exchange device; Described outlet switch and working time control unit comprise supply socket, operation exhibited light and control set and display screen working time.
Further, described water purifying and sterilizing device is fish culture water, recreational water, domestic water or purifying of drinking water sterilizing unit.
Owing to adopting technique scheme, the utility model at least has the following advantages:
(1) ozone gas-liquid exchange device of the present utility model is according to the principle of nature wave and waterfall inflation plain boiled water, adopt novel non-high-pressure spray towing type ozone gas-liquid mass transfer method, the mobile weep traction bottom ozone bubbling aerator ozone out of the normal pressure high speed split that utilizes just/inversed umbrella type rotating gas-liquid transfer device to form effectively enters in water, it is the normal pressure modified version of high-pressure spray, improved the stability of gas dissolved in water, gas-liquid mass transfer efficiency and utilization ratio are high.
(2) water purifying and sterilizing device of the present utility model, ozone tail gas is few, and absorbing off-gas ozone decomposition catalyst gac manganese post and ceramic PTC thermal degradation device efficiency are high, and safe odorless oxygen is revealed.
(3) water purifying and sterilizing device of the present utility model can adopt air source or source of oxygen to manufacture ozone, with low cost, convenient sources.
(4) water purifying and sterilizing device of the present utility model, can in establish active carbon filtering device, be a kind of efficient, the water purifying and sterilizing device that low-cost, security is good.Adopt ozone in conjunction with the gac water treatment method, especially rear end arranges activated-carbon device, ozone is further purified waste water at gac interface formation advanced oxidation, and utmost point easy bacteria-developing while having overcome use activated carbon treatment water forms bacterial biof iotalm BIOFILM and the problem that causes the secondary pollution of water.
(5) water purifying and sterilizing device of the present utility model adopt the outlet switch and working time control unit, switch and the working time of described active carbon filtering device and ozone gas-liquid exchange device can be controlled.
(6) water purifying and sterilizing device of the present utility model be applicable to various large-scale aquarium water purifying sterilizings, support fish tank water purifying sterilizing, rearing pond water purifying sterilizing, life in the countryside water and drink water purifying sterilization, household water and tap water dechlorination purifying sterilizing, city recreational water (water slide, fountain, swimming pool) purifying sterilizing.
The accompanying drawing explanation
Above-mentioned is only the general introduction of technical solutions of the utility model, and in order to better understand technique means of the present utility model, below in conjunction with accompanying drawing and embodiment, the utility model is described in further detail.
Figure 1A is ozone gas-liquid exchange device structural representation of the present utility model (positive umbellate form).
Figure 1B is ozone gas-liquid exchange device structural representation of the present utility model (inversed umbrella type).
Fig. 2 A is inversed umbrella type rotating gas-liquid transfer device structural representation, and the positive umbellate form ozone gas-liquid exchange device structure of Figure 1A is with to fall structure and the cross section, A-A place of umbrella in Fig. 2 A and Fig. 2 B consistent, no longer separately accompanying drawing.
Fig. 2 B is A-A place sectional view in Fig. 2 A.
Fig. 3 A is the water purifying and sterilizing device structural representation that the utility model comprises ozone gas-liquid exchange device (positive umbellate form) and active carbon filtering device.
Fig. 3 B is the water purifying and sterilizing device structural representation that the utility model comprises ozone gas-liquid exchange device (inversed umbrella type) and active carbon filtering device.
Fig. 4 is Inlet and outlet water road technique route (center is sump) schematic diagram.
Fig. 5 is ozonizer modular construction schematic diagram.
Fig. 6 is that ozone enters gas technological line (terminal is the gas storehouse) schematic diagram.
Fig. 7 is that ozone tail gas is eliminated the modular construction schematic diagram.
Fig. 8 is ozone tail gas technological line (starting point is the gas storehouse) schematic diagram.
Fig. 9 is the active carbon filtering device structural representation.
Figure 10 be the outlet switch and working time the control unit schematic diagram.
Figure 11 combines to use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, oxygenerator, outlet switch and control unit processing working time fish-culture sewage schematic diagram.
Figure 12 combines to use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, outlet switch and control unit processing working time domestic water schematic diagram.
Figure 13 combines to use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, post active carbon filtration unit, outlet switch and control unit processing working time drinking-water schematic diagram.
Figure 14 be combine use ozone gas-liquid exchange device, oxygenerator, preposition activated charcoal filtration unit, post active carbon filtration unit, switch and working time control unit fast processing recreational water schematic diagram.
Embodiment
Refer to shown in Figure 1A, ozone gas-liquid exchange device for a kind of structure formation, comprise shell 24, drive-motor 21 and ozone bubbling aerator 23, wherein, drive-motor 21 is fixed on shell 24 tops, shell 24 surrounds and forms the gas-liquid exchange storehouse that comprises 214He bottom, gas storehouse, top sump 215, and ozone bubbling aerator 23 is fixed in sump 215; The ozone gas-liquid exchange device also comprises positive umbellate form rotating gas-liquid transfer device 22, and positive umbellate form rotating gas-liquid transfer device 22 comprises the umbrella handle axle and is arranged on the positive canopy of umbrella handle axle lower end; Drive-motor 21 is connected with the upper end of umbrella handle axle, and positive canopy is positioned at sump, and ozone bubbling aerator 23 is positioned at the umbrella mouth below of positive canopy.
Please coordinate shown in Figure 1B, ozone gas-liquid exchange device for another kind of structure formation, on the basis of Figure 1A structure, positive umbellate form rotating gas-liquid transfer device 22 wherein replaces with inversed umbrella type rotating gas-liquid transfer device 22a, now need to set up water conservancy diversion enhancing tube 9, inversed umbrella type rotating gas-liquid transfer device 22a comprises the umbrella handle axle and is arranged on the canopy that falls of umbrella handle axle lower end; Drive-motor 21 is connected with the upper end of umbrella handle axle, the canopy that falls of inversed umbrella type rotating gas-liquid transfer device 22a is positioned at sump 215, and the umbrella top of canopy is positioned at the top end opening place of water conservancy diversion enhancing tube 9, water conservancy diversion enhancing tube 9 is fixed in sump 215, and ozone bubbling aerator 23 is arranged on the bottom end opening place of water conservancy diversion enhancing tube 9.
Please coordinate and consult Fig. 2 A, 2B, inversed umbrella type rotating gas-liquid transfer device comprises umbrella handle axle 221 and is arranged on the canopy that falls of umbrella handle axle 221 lower ends; Described canopy comprises umbellate form retaining plate 222, is provided with a plurality of ventilating pits 225 on umbellate form retaining plate 222, in umbellate form retaining plate 222 outsides, by standing bolt 224, laminated plastics or metal hole pattern 223 is installed.
Ozone bubbling aerator 23 is for to have a plurality of annular hollow ventpipes that are uniformly distributed eyelet, and in this example, eye diameter is set to 0.5mm.In order to make from bottom ozone bubbling aerator 23, ozone gas stroke out is long and utilization ratio is high, and gas-liquid exchange storehouse is preferably thin and tall type.
Please continue to consult Figure 1A, shell 24 tops of ozone gas-liquid exchange device are provided with water inlet 25 and ozone tail gas entrance 210, water inlet 25 front ends are communicated with inhalent siphon, and inhalent siphon is provided with into water pump and enters electromagnetic valve for water pump 28, enters the water pump front end and is provided with into water pump water inlet 213; Shell 24 bottoms are provided with water outlet 26, and described water outlet 26 rear ends are communicated with rising pipe, and rising pipe is provided with out water pump 27, goes out water pump 27 rear ends and sets out pump outlet 211; Gas storehouse 214 is provided with water-level detecting function unit 29 with the intersection of sump 215, is arranged on the sidewall of shell 24; Water-level detecting function unit 29 comprises water level float and dry-reed tube magnetic force water level control post; described water level is controlled post and is set to level Four; be that first step water level is that water level is shut down in the warning of water overfill; second stage water level is for bringing into operation and continuing operating water level; third stage water level is for adding water and continuing operating water level, and fourth stage water level is the lack of water water level out of service of reporting to the police.Described water-level detecting function unit 29 also can be set to the formation of water level monitoring probe.Coordinate shown in Fig. 4, the Inlet and outlet water route is: enter the sump 215 → water outlet 26 in water pump water inlet 213 → enter water pump → gas-liquid exchange storehouse → go out water pump 27 → go out pump outlet 211.
Please coordinate and consult Fig. 3, the utility model also provides the water that comprises ozone gas-liquid exchange device 2 purifying and sterilizing device, and described water purifying and sterilizing device also comprises ozonizer unit 3, ozone tail gas elimination unit 4; Ozonizer unit 3 is communicated with ozone bubbling aerator 23, and ozone tail gas is eliminated unit 4 and is communicated with gas storehouse 214.Described ozone gas-liquid exchange device 2, ozonizer unit 3, ozone tail gas are eliminated unit 4 and are installed in a main body cover 1, and at main body cover 1 inwall, radiator fan 8 also be installed.Further, main body cover 1 inwall also is provided with the electric control gear 5 of ozone gas-liquid exchange device 2, for controlling aforementioned water-level detecting function unit 29 and entering electromagnetic valve for water pump 28.
Refer to shown in Fig. 5 a plurality of ozonizer groups that the ozonizer unit comprises air drying agent post 31 and is communicated with air drying agent post 31, a plurality of ozonizer groups whiles or alternate run; 2 the ozonizer groups of take are example, ozonizer group A32 and ozonizer group B33 comprise respectively the air pump 321,331 be communicated with air drying agent post 31 and ozonizer A322 and the ozonizer B332 be communicated with respectively with air pump 321,331, ozonizer A, B inside are equipped with radiator fan 34, be respectively equipped with the ozone outlet pipe on ozonizer A322 and ozonizer B332, on outlet pipe respectively correspondence be provided with cooling gas check valve 323,333; Air drying agent post 31 front ends are connected with the oxygenerator (not shown) by air intake 311 or air drying agent post 31 is direct and air communication.Coordinate shown in Fig. 6, ozone enters the gas circuit line and is: air intake 311 → dry post 31 → air pump 321/331 → ozonizer 322/332 → cooling gas check valve 323/333 → gas-liquid exchange Qi storehouse, storehouse 214.
Refer to shown in Fig. 7, ozone tail gas is eliminated unit and is comprised interconnected ceramic PTC thermal degradation device 42 and absorbing off-gas ozone decomposition catalyst gac manganese post 41, and ceramic PTC thermal degradation device 42 is arranged on the front end of charcoal manganese post 41.Coordinate shown in Fig. 8, the ozone tail gas route is: gas-liquid exchange Qi storehouse, storehouse 214 → gas inlet, 210 → ceramic PTC thermal degradation device, 42 → charcoal manganese post, 41 → tail gas outlet 43.
Further, please coordinate and consult Fig. 3, at the front end of ozone gas-liquid exchange device 2, the active carbon filtering device 6 be communicated with ozone gas-liquid exchange device 2 can also be set.The Huo rear and front end, rear end that described active carbon filtering device 6 also can be arranged on ozone gas-liquid exchange device 2 arranges simultaneously.
Refer to shown in Fig. 9, active carbon filtering device comprises body fuselage 61, is arranged on water inlet 62, water outlet 63, sewage draining exit 64 and base 65 on body fuselage 61; Water inlet 62 front ends are provided with into water pump 611, describedly enter on water pump 611 to be provided with into water pump water inlet 613; Water inlet 62 rear ends are communicated with into water mixing chamber 66, enter water mixing chamber 66 rear ends and are provided with filter cotton A67; Water outlet 63 rear ends are provided with and distribute the mouth of a river 614, and water outlet 63 front ends are communicated with water outlet mixing chamber 610, and water outlet mixing chamber 610 front ends are provided with filter cotton B69; Between described filter cotton A67, B69, activated carbon filtration post 68 is set, is filled in described body fuselage 61 inside.
Further, please coordinate and consult Fig. 3, water purifying and sterilizing device of the present utility model also comprise the outlet switch and working time control unit 7, for controlling active carbon filtering device 6 and ozone gas-liquid exchange device 2.As shown in figure 10, the outlet switch and working time control unit comprise supply socket 71, operation exhibited light 72 and control set and display screen 73 working time.
Please coordinate and consult Figure 11-14, water purifying and sterilizing device of the present utility model is applicable to various large-scale aquarium water purifying sterilizings, supports fish tank water purifying sterilizing, rearing pond water purifying sterilizing, life in the countryside water and drink water purifying sterilization, household water and tap water dechlorination purifying sterilizing, city recreational water (water slide, fountain, swimming pool) purifying sterilizing.
Below example further illustrates the beneficial effects of the utility model by experiment:
Experimental example 1
Purpose: test water purifying and sterilizing device of the present utility model to the water purification effect of breeding fish.
Method: use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, oxygenerator, switch and control unit working time (Figure 11) to process the fish-culture sewage in fishpond/cylinder 10, observation is not used refining plant and is used water clarity and the colour-change of refining plant.
The every day operation of table 1 90% oxygen source ozone gac water-purification plant is safeguarded 1.8 tons of water high-density fish culture cylinders (approximately 70 long aquarium fish of 10-15cm) water clarity and colour-change in 4 hours
Conclusion: water purifying and sterilizing device of the present utility model can be used for purifying large-scale aquarium water fully.
Experimental example 2
Purpose: test the decontamination effect improving of water purifying and sterilizing device of the present utility model to organic substance in the water of breeding fish.
Method: use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, oxygenerator, switch and control unit working time (Figure 11) to process fish-culture sewage, measure the numerical value change that purifies COD in the water of front and back, to judge its decontamination effect improving to organic substance in water.
COD value delta data recorder (mg/L) in table 2 water
Conclusion: water purifying and sterilizing device of the present utility model can purify the organic pollution materials in large-scale aquarium water.
Experimental example 3
Purpose: test the decontamination effect improving of water purifying and sterilizing device of the present utility model to microorganism in large-scale aquarium water.
Method: use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, oxygenerator, switch and control unit working time (Figure 11) to process fish-culture sewage, measure the content that purifies microorganism in the water of front and back, to judge its decontamination effect improving to microorganism in water.
The data variation recorder (cfu/ml) of content of microorganisms in table 3 water
Conclusion: use air source and water purifying and sterilizing device of the present utility model, can 100% remove microorganism in water.
Experimental example 4
Purpose: test water purifying and sterilizing device of the present utility model to mountain stream water purification effect.
Method: use ozone gas-liquid exchange device, preposition activated charcoal filtration unit, post active carbon filtration unit, switch and control unit working time (Figure 13) to process mountain stream water and drink, measure the various indexs of water before and after purifying, judgement water purification effect.
Table 4 air source ozone gac water-purification plant mountain stream water purifies detected result
Conclusion: use air source ozone, utilize water purifying and sterilizing device of the present utility model to purify mountain stream water, can reach drinking water standard.
Experimental example 5
Purpose: test water purifying and sterilizing device of the present utility model to city recreational water slide water purification effect.
Method: the city recreational water slide water that uses ozone gas-liquid exchange device, oxygenerator, preposition activated charcoal filtration unit, post active carbon filtration unit, switch and many people of control unit working time (Figure 14) fast processing to use every day, observation is not used refining plant and is used water clarity and the colour-change of refining plant.
Table 5 is used oxygenerator that 90% oxygen and ozone and activated carbon water-purification plant are provided, and at interval of operation in 1 hour 1 hour, safeguards 6 tons of city recreational water slide water clarities and colour-change
Conclusion: the water purifying and sterilizing device of this utility model can be used for purifying city recreational water slide water fully.
Experimental example 6
Purpose: just/inversed umbrella type rotating gas-liquid transfer device and just/inversed umbrella type rotating gas-liquid transfer device ozone gas-liquid exchange comparative studies.
Method: relatively two types of the ozone gas-liquid exchange device, ozone gas-liquid exchange velocity and the utilization ratio of just/inversed umbrella type rotating gas-liquid transfer device and just/inversed umbrella type rotating gas-liquid transfer device.
Table 6 just/inversed umbrella type gas-liquid transfer device and just/inversed umbrella type gas-liquid transfer device comparative result (24 degree)
Conclusion: Multilayer Network cover the umbrella top just/inversed umbrella type rotating gas-liquid transfer device all forms the mobile weep of normal pressure high speed split, the ozone gas port gas ozone with the air source manufacture out of bottom ozone bubbling aerator out in traction top effectively enters in water, is all normal pressure modified version and the novel non-high pressure towing type ozone gas-liquid mass transfer method of high-pressure spray; Thin and tall type gas-liquid exchange storehouse is in conjunction with bottom ozone bubbling aerator and just/inversed umbrella type rotating gas-liquid transfer device ozone gas stroke is long and utilization ratio is slightly high, and effectively the water level amplitude becomes large simultaneously, is conducive to water level control and minimizing magnetic valve open frequency.
Experimental example 7
Purpose: ozone gas-liquid exchange device of the present utility model, preposition activated charcoal filtration unit, post active carbon filtration unit, oxygenerator, switch and control unit different application mode of connection signal working time.
Method: use ozone gas-liquid exchange device of the present utility model, preposition activated charcoal filtration unit, post active carbon filtration unit, oxygenerator, switch and working time control unit, process water and fish-culture sewage in the connection as shown in Figure 11,12,13,14, Figure 11 is used the ozone gas-liquid exchange device, preposition activated charcoal filtration unit, oxygenerator, switch and control unit processing working time fish-culture sewage, Figure 12 is used the ozone gas-liquid exchange device, preposition activated charcoal filtration unit, switch and control unit processing working time domestic water, Figure 13 is used the ozone gas-liquid exchange device, preposition activated charcoal filtration unit, the post active carbon filtration unit, switch and control unit processing working time drinking-water, Figure 14 is used the ozone gas-liquid exchange device, oxygenerator, preposition activated charcoal filtration unit, the post active carbon filtration unit, switch and working time control unit fast processing recreational water.
Result: all normal effectively work of fish-culture sewage, domestic water, recreational water, drinking-water is processed in the connection as shown in Figure 11,12,13,14.
The all normal effectively work of fish-culture sewage, domestic water, recreational water, drinking-water is processed in connection shown in conclusion: Figure 11,12,13,14.
Experimental example 8
Purpose: determine ozone gas-liquid exchange device partial parameters of the present utility model.
Method: use the ozone gas-liquid exchange device under different condition, determine operation parameter.
Result: in Table 7.
Table 7 ozone gas-liquid exchange device parameter
Conclusion: ozone gas-liquid exchange device of the present utility model is used stable under different rated conditions.
The foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although with reference to previous embodiment, the utility model is had been described in detail, for a person skilled in the art, its technical scheme that still can put down in writing previous embodiment is modified, or part technical characterictic wherein is equal to replacement.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (13)
1. an ozone gas-liquid exchange device, it is characterized in that, comprise shell, drive-motor, ozone bubbling aerator, described drive-motor is fixed on cover top portion, described shell surrounds and forms the gas-liquid exchange storehouse that comprises Qi Canghe bottom, top sump, and described ozone bubbling aerator is fixed in sump;
Also comprise positive umbellate form rotating gas-liquid transfer device, described positive umbellate form rotating gas-liquid transfer device comprises the umbrella handle axle and is arranged on the positive canopy of umbrella handle axle lower end; Described drive-motor is connected with the upper end of umbrella handle axle, and described positive canopy is positioned at sump, and described ozone bubbling aerator is positioned at the umbrella mouth below of positive canopy;
Or also comprise that inversed umbrella type rotating gas-liquid transfer device and water conservancy diversion enhancing tube, described inversed umbrella type rotating gas-liquid transfer device comprise the umbrella handle axle and be arranged on the canopy that falls of umbrella handle axle lower end; Described drive-motor is connected with the upper end of umbrella handle axle, described canopy is positioned at sump, and the described umbrella top of canopy is positioned at the top end opening place of water conservancy diversion enhancing tube, and described water conservancy diversion enhancing tube is fixed in sump, and described ozone bubbling aerator is arranged on the bottom end opening place of water conservancy diversion enhancing tube.
2. ozone gas-liquid exchange device according to claim 1, is characterized in that, described gas-liquid exchange storehouse is thin and tall type gas-liquid exchange storehouse.
3. ozone gas-liquid exchange device according to claim 1, it is characterized in that, described positive canopy or the canopy of canopy of falling comprise the umbellate form retaining plate, be provided with a plurality of ventilating pits on described umbellate form retaining plate, and the described umbellate form retaining plate outside are installed with laminated plastics or metal hole pattern.
4. ozone gas-liquid exchange device according to claim 1, is characterized in that, described ozone bubbling aerator is to have a plurality of annular hollow ventpipes that are uniformly distributed eyelet.
5. ozone gas-liquid exchange device according to claim 1, is characterized in that, described shell top is provided with water inlet, and described water inlet front end is communicated with inhalent siphon, and described inhalent siphon is provided with into water pump and enters electromagnetic valve for water pump; Described shell bottom is provided with water outlet, and described water outlet rear end is communicated with rising pipe, and described rising pipe is provided with out water pump;
The intersection of described gas storehouse and sump is provided with the water-level detecting function unit, is arranged on the sidewall of described shell; Described water-level detecting function unit comprises water level float and dry-reed tube magnetic force water level control post, described water level is controlled post and is set to level Four, be that first step water level is that water level is shut down in the warning of water overfill, second stage water level is for bringing into operation and continuing operating water level, third stage water level is for adding water and continuing operating water level, and fourth stage water level is the lack of water water level out of service of reporting to the police;
Described ozone gas-liquid exchange device also comprises electric control gear, and described electric control gear is controlled described water-level detecting function unit and entered electromagnetic valve for water pump.
6. a water purifying and sterilizing device, is characterized in that, comprises the described ozone gas-liquid exchange device of claim 1-5 any one, also comprises ozonizer unit, ozone tail gas elimination unit; Described ozonizer unit is communicated with ozone bubbling aerator, and ozone tail gas is eliminated Yu Qi storehouse, unit and is communicated with.
7. water purifying and sterilizing device according to claim 6, it is characterized in that, a plurality of ozonizer groups that described ozonizer unit comprises the air drying agent post and is communicated with the air drying agent post, described ozonizer group comprises the air pump be communicated with the air drying agent post and the ozonizer be communicated with air pump, described ozonizer inside is provided with radiator fan, described ozonizer is provided with the ozone outlet pipe, and described outlet pipe is provided with cooling gas check valve; Described a plurality of ozonizer group while or alternate run;
Described air drying agent post front end is connected with oxygenerator or the air drying agent post is direct and air communication.
8. water purifying and sterilizing device according to claim 6, is characterized in that, described ozone tail gas is eliminated unit and comprised interconnected ceramic PTC thermal degradation device and charcoal manganese post, and described ceramic PTC thermal degradation device is arranged on the front end of charcoal manganese post.
9. water purifying and sterilizing device according to claim 6, it is characterized in that, described ozone gas-liquid exchange device, ozonizer unit, ozone tail gas are eliminated unit and are installed in a main body cover, and at described main body cover inwall, radiator fan also be installed.
10. water purifying and sterilizing device according to claim 6, is characterized in that, also comprises the active carbon filtering device that is arranged on end before or after the ozone gas-liquid exchange device, is communicated with the ozone gas-liquid exchange device.
11. water purifying and sterilizing device according to claim 10 is characterized in that described active carbon filtering device comprises body fuselage, is arranged on water inlet, water outlet, sewage draining exit and base on body fuselage; Described water inlet front end is provided with into water pump, and the water inlet rear end is communicated with into the water mixing chamber, describedly enters water mixing chamber rear end and is provided with filter cotton A; Described water outlet rear end is provided with and distributes the mouth of a river, and the water outlet front end is communicated with the water outlet mixing chamber, and described water outlet mixing chamber front end is provided with filter cotton B; Between described filter cotton A, B, the activated carbon filtration post is set, is filled in described body fuselage inside.
12. water purifying and sterilizing device according to claim 10, is characterized in that, also comprise the outlet switch and working time control unit, for controlling described active carbon filtering device and ozone gas-liquid exchange device; Described outlet switch and working time control unit comprise supply socket, operation exhibited light and control set and display screen working time.
13. according to the described water purifying and sterilizing device of claim 6-12 any one, it is characterized in that, described water purifying and sterilizing device is fish culture water, recreational water, domestic water or purifying of drinking water sterilizing unit.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106536808A (en) * | 2014-07-23 | 2017-03-22 | Bsh家用电器有限公司 | Household appliance comprising mist circuit for conducting ozone-containing mist |
| CN107010760A (en) * | 2017-05-26 | 2017-08-04 | 青岛华水节能环保科技有限公司 | The deep treatment method and device of Drinking Water |
| CN108529737A (en) * | 2018-05-18 | 2018-09-14 | 南通劲凌智能科技有限公司 | A kind of aerating oxidation tower and its method for groundwater treatment |
| CN108675520A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of sterilization settling system and its method for water process |
| CN108675491A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of dosing aerating system for water body purification |
| CN108675492A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of sewage aeration processing system |
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2013
- 2013-07-11 CN CN 201320411844 patent/CN203360086U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106536808A (en) * | 2014-07-23 | 2017-03-22 | Bsh家用电器有限公司 | Household appliance comprising mist circuit for conducting ozone-containing mist |
| CN107010760A (en) * | 2017-05-26 | 2017-08-04 | 青岛华水节能环保科技有限公司 | The deep treatment method and device of Drinking Water |
| CN108529737A (en) * | 2018-05-18 | 2018-09-14 | 南通劲凌智能科技有限公司 | A kind of aerating oxidation tower and its method for groundwater treatment |
| CN108675520A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of sterilization settling system and its method for water process |
| CN108675491A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of dosing aerating system for water body purification |
| CN108675492A (en) * | 2018-05-18 | 2018-10-19 | 南通劲凌智能科技有限公司 | A kind of sewage aeration processing system |
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