CN107161955A - High-concentrated ozone liquid generating means - Google Patents
High-concentrated ozone liquid generating means Download PDFInfo
- Publication number
- CN107161955A CN107161955A CN201710449916.9A CN201710449916A CN107161955A CN 107161955 A CN107161955 A CN 107161955A CN 201710449916 A CN201710449916 A CN 201710449916A CN 107161955 A CN107161955 A CN 107161955A
- Authority
- CN
- China
- Prior art keywords
- ozone
- communicated
- generation unit
- generating means
- air inlet
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/10—Preparation of ozone
- C01B13/11—Preparation of ozone by electric discharge
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2201/00—Preparation of ozone by electrical discharge
- C01B2201/10—Dischargers used for production of ozone
- C01B2201/12—Plate-type dischargers
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2201/00—Preparation of ozone by electrical discharge
- C01B2201/60—Feed streams for electrical dischargers
- C01B2201/64—Oxygen
Abstract
The invention discloses high-concentrated ozone liquid generating means, including air inlet pipe, pump machine, fan housing, ozone generation unit, water tank and the muffler being sequentially communicated；The muffler is communicated in air inlet pipe；The one end of the air inlet pipe away from pump machine is communicated in oxygen cylinder；The size that the fan housing is communicated in pump machine is matched with the size of pump machine air outlet；The size that the fan housing is communicated in ozone generation unit is matched with the size of ozone generation unit.High-concentrated ozone liquid generating means of the present invention, by setting said apparatus, concentration necessary can be met by realizing the solution prepared and need not processing again, while ozone can be passed through water tank repeatedly, and then reduced the discharge capacity of ozone, be conducive to health.
Description
Technical field
The present invention relates to field of medical products, and in particular to high-concentrated ozone liquid generating means.
Background technology
Ozone (O3) it is oxygen (O2) allotrope, it is a kind of light blue gas with special odor.Molecule knot
Structure is triangular in shape, and bond angle is 116 °, and its density is 1.5 times of oxygen, and the solubility in water is 10 times of oxygen.Ozone is one
Kind of strong oxidizer, its oxidation-reduction potential in water is 2.07eV, is only second to fluorine (2.5eV), its oxidability is higher than chlorine
(1.36eV) and chlorine dioxide (1.5eV), can destroy the cell membrane of decomposing bacteria, and soon diffusion penetrates into intracellular, oxidation point
Glucose oxidase etc., directly can also have an effect with bacterium, virus necessary to solving bacterium internal oxidation glucose, destroy
Cell, ribonucleic acid (RNA), decompose the macromolecular polymerics such as DNA (DNA), RNA, protein, lipid and polysaccharide
Thing, the metabolism and reproductive process for making bacterium is destroyed.It is this process caused by the fracture of cell membrane that bacterium is killed by ozone
It is referred to as cell lysis, is due to that cell can not possibly regenerate under conditions of dissipation caused by cytoplasm is crushed in water.Should
Different from hypochlorous acid class disinfectant when pointing out, the sterilizing ability of ozone is not influenceed by pH value change and ammonia, its sterilizing ability ratio
Chlorine is big 600-3000 times, and its sterilizing, disinfective action is almost what is instantaneously occurred, in Measuring Ozone Concentration in Water 0.3-2mg/L,
Can be with lethal bacterium in 0.5-1min.Ozone Water needed for reaching identical sterilization effect (as made Escherichia coli killing rate up to 99%)
Pharmaceutical quantities are only the 0.0048% of chlorine.Carried out disinfection so medical science sterilization now is a large amount of using ozone solution.
However, existing ozone solution preparation method, the solution prepared, which needs to carry out processing again, could meet concentration
It is required that, while also the ozone that solution is not completely dissolved in can be directly discharged into air, and toxicity that ozone has and corrosivity meeting
Do harm to huamn body.
The content of the invention
The technical problems to be solved by the invention are existing ozone solution preparation methods, and the solution prepared needs to carry out
Processing could meet concentration requirement again, and dirt is caused while also the ozone that solution is not completely dissolved in can be directly discharged into air
Dye, it is therefore intended that high-concentrated ozone liquid generating means are provided, solved the above problems.
The present invention is achieved through the following technical solutions：
High-concentrated ozone liquid generating means, including be sequentially communicated air inlet pipe, pump machine, fan housing, ozone generation unit, water tank
And muffler；The muffler is communicated in air inlet pipe；The one end of the air inlet pipe away from pump machine is communicated in oxygen cylinder；The fan housing
The size for being communicated in pump machine is matched with the size of pump machine air outlet；The size that the fan housing is communicated in ozone generation unit is matched with
The size of ozone generation unit.
In the prior art, ozone solution preparation method, the solution prepared, which needs to carry out processing again, could meet concentration
It is required that, while also the ozone that solution is not completely dissolved in can be directly discharged into air, and toxicity that ozone has and corrosivity meeting
Do harm to huamn body.When the present invention is applied, the oxygen in oxygen cylinder is pumped into fan housing by pump machine by air inlet pipe, and fan housing is by oxygen
Each ozone generation unit is dispersed to, ozone is made in ozone generation unit, and then ozone enters water tank, and is dissolved in water tank
Solution, then cooled via return air pipe are imported in air inlet pipe, because ozone can not be dissolved completely in solution, so the gas meeting in muffler
There is certain ozone content, these gases are again introduced into ozone generation unit through air inlet pipe and pump machine, ozone concentration can be further
Improve, then enter back into water tank and be dissolved in solution, so circulation, effectively raise the concentration of ozone solution, and ozone meeting
Passed through water tank repeatedly, and then reduce the discharge capacity of ozone, be conducive to health.The present invention by setting said apparatus,
Concentration necessary can be met by realizing the solution prepared and need not processing again, while ozone can be passed through water tank repeatedly, be entered
And the discharge capacity of ozone is reduced, be conducive to health.
Further, the ozone generation unit includes two collector plates, two dielectrics, outlet side, gas outlet, air inlets
End, air inlet and insulating trip；Described two collector plates are arranged oppositely, and set two dielectrics on two collector plates respectively；Institute
State outlet side and be arranged at one end that ozone generation unit is communicated in water tank, and gas outlet is set on outlet side；The inlet end is set
One end that ozone generation unit is communicated in fan housing is placed in, and air inlet is set on inlet end；The different ozone generation unit
Between adjacent set insulating trip.
When the present invention is applied, oxygen passes through between two collector plates, and two collector plates and two dielectrics produce strong electric discharge,
So as to convert the oxygen to ozone, this mode is in the ozone production structure of cycle arrangement, and efficiency is very high, and by oxygen
The influence of gas concentration less so that over numerous cycles, the concentration of ozone improve and during the decline of the concentration of oxygen, can also
Effective production ozone, and improve the concentration of ozone solution.
Further, the dielectric uses rutile of the titania weight content more than 95%.
Further, the collector plate uses tungsten.
Further, the insulating trip uses porous ceramics.
When the present invention is applied, porous ceramics between different ozone generation units to realizing insulated heat.
The present invention compared with prior art, has the following advantages and advantages：
1st, high-concentrated ozone liquid generating means of the present invention, by setting said apparatus, realize the solution prepared and are not required to
Concentration necessary can be met by processing again, while ozone can be passed through water tank repeatedly, and then reduce the discharge capacity of ozone, have
Beneficial to health；
2nd, high-concentrated ozone liquid generating means of the present invention, due to preparing ozone, over numerous cycles, ozone by collector plate
Concentration improve and during the decline of the concentration of oxygen, it is possibility to have the production ozone of effect, and improve the concentration of ozone solution.
Brief description of the drawings
Accompanying drawing described herein is used for providing further understanding the embodiment of the present invention, constitutes one of the application
Point, do not constitute the restriction to the embodiment of the present invention.In the accompanying drawings：
Fig. 1 is schematic structural view of the invention.
Mark and corresponding parts title in accompanying drawing：
1- ozone generation units, 2- water tanks, 3- fan housings, 4- pump machines, 5- air inlet pipe, 6- mufflers, 11- collector plates, 12- electricity
Medium, 13- outlet sides, 14- gas outlets, 15- inlet ends, 16- air inlets, 17- insulating trips.
Embodiment
For the object, technical solutions and advantages of the present invention are more clearly understood, with reference to embodiment and accompanying drawing, to this
Invention is described in further detail, and exemplary embodiment and its explanation of the invention is only used for explaining the present invention, does not make
For limitation of the invention.
Embodiment
As shown in figure 1, high-concentrated ozone liquid generating means of the present invention, including be sequentially communicated air inlet pipe 5, pump machine 4, fan housing
3rd, ozone generation unit 1, water tank 2 and muffler 6；The muffler 6 is communicated in air inlet pipe 5；The air inlet pipe 5 is away from pump machine 4
One end be communicated in oxygen cylinder；The size that the fan housing 3 is communicated in pump machine 4 is matched with the size of the air outlet of pump machine 4；The fan housing
3 sizes for being communicated in ozone generation unit 1 are matched with the size of ozone generation unit 1.The ozone generation unit 1 includes two
Collector plate 11, two dielectrics 12, outlet side 13, gas outlet 14, inlet end 15, air inlet 16 and insulating trip 17；It is described two
Collector plate 11 is arranged oppositely, and sets two dielectrics 12 on two collector plates 11 respectively；The outlet side 13 is arranged at ozone
Generation unit 1 is communicated in setting gas outlet 14 on one end of water tank 2, and outlet side 13；The inlet end 15 is arranged at ozone life
Setting air inlet 16 on one end of fan housing 3, and inlet end 15 is communicated in into unit 1；Between the different ozone generation unit 1
Adjacent sets insulating trip 17.Rutile of the dielectric 12 using titania weight content more than 95%.The collection
Electric piece 11 uses tungsten.The insulating trip 17 uses porous ceramics.
When the present embodiment is implemented, the oxygen in oxygen cylinder is pumped into fan housing 3 by pump machine 4 by air inlet pipe 5, and fan housing 3 is by oxygen
Each ozone generation unit 1 is dispersed to, ozone is made in ozone generation unit 1, then ozone enters water tank 2, and is dissolved in water tank 2
In solution, then cooled via return air pipe 6 import air inlet pipe 5 in, because ozone can not be dissolved completely in solution, so in muffler 6
Gas have certain ozone content, these gases are again introduced into ozone generation unit 1 through air inlet pipe 5 and pump machine 4, and ozone is dense
Degree can be improved further, then entered back into water tank 2 and be dissolved in solution, so circulation, effectively raise the concentration of ozone solution,
And ozone can be passed through water tank 2 repeatedly, and then the discharge capacity of ozone is reduced, be conducive to health.The present invention is by setting
Said apparatus is put, concentration necessary can be met by realizing the solution prepared and need not processing again, while ozone can be by repeatedly
By water tank 2, and then the discharge capacity of ozone is reduced, be conducive to health.Oxygen passes through between two collector plates 11, two
Collector plate 11 and two dielectrics 12 produce strong electric discharge, so as to convert the oxygen to ozone, this mode is in the smelly of cycle arrangement
In oxygen production structure, efficiency is very high, and is influenceed less by oxygen concentration, so that over numerous cycles, ozone
Concentration improve and during the decline of the concentration of oxygen, it is possibility to have the production ozone of effect, and improve the concentration of ozone solution.
Above-described embodiment, has been carried out further to the purpose of the present invention, technical scheme and beneficial effect
Describe in detail, should be understood that the embodiment that the foregoing is only the present invention, be not intended to limit the present invention
Protection domain, within the spirit and principles of the invention, any modification, equivalent substitution and improvements done etc. all should be included
Within protection scope of the present invention.
Claims (5)
1. high-concentrated ozone liquid generating means, it is characterised in that including the air inlet pipe (5) being sequentially communicated, pump machine (4), fan housing
(3), ozone generation unit (1), water tank (2) and muffler (6)；The muffler (6) is communicated in air inlet pipe (5)；The air inlet
The one end of pipe (5) away from pump machine (4) is communicated in oxygen cylinder；The size that the fan housing (3) is communicated in pump machine (4) is matched with pump machine
(4) size of air outlet；The size that the fan housing (3) is communicated in ozone generation unit (1) is matched with ozone generation unit (1)
Size.
2. high-concentrated ozone liquid generating means according to claim 1, it is characterised in that the ozone generation unit (1)
Including two collector plates (11), two dielectrics (12), outlet side (13), gas outlet (14), inlet end (15), air inlets (16)
With insulating trip (17)；Described two collector plates (11) are arranged oppositely, and set two dielectrics respectively on two collector plates (11)
(12)；The outlet side (13) is arranged on one end that ozone generation unit (1) is communicated in water tank (2), and outlet side (13) and set
Put gas outlet (14)；The inlet end (15) is arranged at one end that ozone generation unit (1) is communicated in fan housing (3), and inlet end
(15) air inlet (16) is set on；Adjacent sets insulating trip (17) between the different ozone generation unit (1).
3. high-concentrated ozone liquid generating means according to claim 2, it is characterised in that the dielectric (12) uses two
Rutile of the titania weight content more than 95%.
4. high-concentrated ozone liquid generating means according to claim 2, it is characterised in that the collector plate (11) uses
Tungsten.
5. high-concentrated ozone liquid generating means according to claim 2, it is characterised in that the insulating trip (17) is using more
Hole ceramics.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710449916.9A CN107161955A (en) | 2017-06-14 | 2017-06-14 | High-concentrated ozone liquid generating means |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710449916.9A CN107161955A (en) | 2017-06-14 | 2017-06-14 | High-concentrated ozone liquid generating means |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107161955A true CN107161955A (en) | 2017-09-15 |
Family
ID=59818696
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710449916.9A Withdrawn CN107161955A (en) | 2017-06-14 | 2017-06-14 | High-concentrated ozone liquid generating means |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107161955A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2556188Y (en) * | 2002-06-05 | 2003-06-18 | 喻湛 | Ozone water preparing machine |
| CN1683237A (en) * | 2004-04-08 | 2005-10-19 | 三菱电机株式会社 | Ozone generating apparatus |
| CN102491278A (en) * | 2011-11-28 | 2012-06-13 | 济南瑞清臭氧设备有限公司 | Ozone discharging tube, ozone discharging chamber and vertical type ozone generating device |
| CN102602895A (en) * | 2011-12-22 | 2012-07-25 | 潍坊博药生物科技有限公司 | Ozone water generating assembly for oral hygiene and facial purification and whitening |
| JP2015166066A (en) * | 2014-03-04 | 2015-09-24 | 国立大学法人東京工業大学 | Ozone dissolving apparatus |
-
2017
- 2017-06-14 CN CN201710449916.9A patent/CN107161955A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2556188Y (en) * | 2002-06-05 | 2003-06-18 | 喻湛 | Ozone water preparing machine |
| CN1683237A (en) * | 2004-04-08 | 2005-10-19 | 三菱电机株式会社 | Ozone generating apparatus |
| CN102491278A (en) * | 2011-11-28 | 2012-06-13 | 济南瑞清臭氧设备有限公司 | Ozone discharging tube, ozone discharging chamber and vertical type ozone generating device |
| CN102602895A (en) * | 2011-12-22 | 2012-07-25 | 潍坊博药生物科技有限公司 | Ozone water generating assembly for oral hygiene and facial purification and whitening |
| JP2015166066A (en) * | 2014-03-04 | 2015-09-24 | 国立大学法人東京工業大学 | Ozone dissolving apparatus |
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| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170915 |