CN107601646A - A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation - Google Patents
A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation Download PDFInfo
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- CN107601646A CN107601646A CN201711063407.9A CN201711063407A CN107601646A CN 107601646 A CN107601646 A CN 107601646A CN 201711063407 A CN201711063407 A CN 201711063407A CN 107601646 A CN107601646 A CN 107601646A
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- retort
- ultrasound
- liquid
- unit based
- bactericidal unit
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000002604 ultrasonography Methods 0.000 title claims abstract description 35
- 230000003647 oxidation Effects 0.000 title claims abstract description 18
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 18
- 230000000844 anti-bacterial effect Effects 0.000 title claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 51
- 230000001954 sterilising effect Effects 0.000 claims abstract description 24
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 18
- 238000002156 mixing Methods 0.000 claims description 16
- 230000000694 effects Effects 0.000 abstract description 14
- 238000005265 energy consumption Methods 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 241001314279 Zoopagales Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000009303 advanced oxidation process reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006854 communication Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001151 other effect Effects 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
Abstract
The invention discloses a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation, including the retort with inlet and liquid outlet, the ultrasound wave vibrating bar and ozone generator that are inserted into retort, the gas outlet of the ozone generator is connected by pipeline with inlet, and liquid subject to sterilization connects also by pipeline with inlet.The arrangement increases sterilization effect, while reduce energy consumption.
Description
Technical field
The present invention relates to the sterilizing field of ultrasonic wave and ozone, more particularly to a kind of going out based on ultrasound-enhanced ozone oxidation
Bacterium device.
Background technology
For ozone because having very strong oxidability (oxidation-reduction potential can reach 2.07V), the reaction time is short, can aoxidize water
The advantages that middle most of organic matter, oxidation can also often be passed through by the core technology as high-level oxidation technology (AOPs), ozone
Cell membrane is destroyed, there is very strong sterilizing ability.
Ultrasonic wave can produce a series of effect in its communication process, when the ul-trasonic irradiation of some strength is in liquid
When, a large amount of cavitation bubbles can be produced, and change with sound wave and change size and moment vanishes and forms cavitation phenomenon.Cavitation can
High temperature (5000k) high pressure (5.0x104kPa) and Strong shear power are produced to microbial cell individual moment, are allowed to inactivate.
Although single ozone process can realize sterilization, the sterilization effect of ozone is decided by the gentle hydrosphere of its concentration
Face, the ozone of high concentration need the equipment of complicated and high operating cost to realize, and due to the extremely strong oxidation of ozone with
The characteristics of non-targeted effect, accessory substance is easily formed so as to cause secondary pollution, therefore needed during using ozone sterilization
Solve the problems, such as how to reduce the ozone of effusion, how to increase mass transfer interface.
Common ultrasonic reactor has a cleaning groove type reactor and luffing rod-type reactor, pending liquid in groove type reactor
Residence time is grown, and reactor volume is larger, easily forms short stream and dead band, can not obtain the higher sound intensity, and sound wave reflection is serious;Become
Width rod-type reactor action scope is small, and detecting head surface is perishable because of collection cavitation.
The sterilization effect of ultrasonic reactor is decided by the energy output size (sound field intensity) and cavitation (air pocket) of its sound wave
The space size (acoustic field uniformity) of effect.High frequency ultrasound (>200kHz) due to technical problems such as power supply, shake plates, equipment is expensive,
Stability is relatively low, no image of Buddha low frequency ultrasound (<High-power equipment 200kHz) is made in industrialization like that, although low frequency ultrasound is straight
It is weak to connect oxidability higher-frequency ultrasound, but the output of the energy of high-strength sound field and high performance-price ratio is especially suitable for being combined other oxidation technologies
(such as ozone), which is realized, strengthens bactericidal effect.
Pre-existing reactors between pulling flow type (Plug flow) reactor and complete mix flow (CSTR),
On the premise of realizing high efficient gas and liquid mass transfer and liquid-liquid transfer, how to reduce reactor residence time, dead band and short stream is reactor
The main target of design.Design difficulty for ozone reactor is to improve gas-liquid mass transfer efficiency, and increases ozone simultaneously with going out
Zoopagales target contact probability;And it is the homogenization of sound field for the design difficulty of ultrasonic reactor, and sterilize target and cavitation
The contact probability in domain.
The content of the invention
It is a primary object of the present invention to provide a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation, gone out using ozone
Bacterium and ultrasonic sterilization are combined, and the advantages of using both, can not only reach more preferable sterilization effect, additionally it is possible to realize energy-conservation
And other effects.
To achieve the above objectives, the technical solution adopted by the present invention is:A kind of sterilizing based on ultrasound-enhanced ozone oxidation
Device, it is characterised in that including the retort with inlet and liquid outlet, the ultrasound wave vibrating bar being inserted into retort,
Ozone generator and the internal gas-liquid mixing pump with rotatable impeller, the delivery outlet and inlet of the gas-liquid mixing pump
Connection, the gas outlet of the ozone generator are connected by pipeline with gas-liquid mixing pump, and the liquid subject to sterilization is also by pipe
Road connects with gas-liquid mixing pump.
Preferably, the inlet is arranged on the bottom of retort, and the liquid outlet is arranged on the bottom of retort, anti-
Answer and guide is additionally provided with tank, the lower end of the guide is fixed on the bottom of retort and corresponding with liquid outlet, and upper end extends to
Close to the top of retort, the opening for the upper end that the liquid outlet passes through guide connects with inlet.
Preferably, at least provided with a ultrasound wave vibrating bar in the guide.
Preferably, the inlet is set relative to the eccentric axis of retort.
Preferably, the ultrasound wave vibrating bar includes being inserted into the ultrasonic transformer of bottom at the top of retort and is fixed on luffing
Ultrasonic transducer at the top of bar, the surface that the ultrasonic transformer is located at the part in retort set multiple annular protrusions.
Preferably, the ultrasound wave vibrating bar has multiple.
Preferably, the retort in axial direction on height and diameter ratio be 2.2~2.5:1.
Compared with prior art, the invention has the advantages that:
1) mode being combined by using ozone and ultrasonic wave is sterilized, and on the one hand can improve the effect of sterilizing,
Energy consumption can be reduced by both interactions simultaneously, another aspect ultrasonic wave can promote the decomposition of ozone, reduce ozone
Discharge, serve the effect of environmental protection;
2) gas-liquid mixing pump is used, ozone is evenly dispersed in liquid subject to sterilization, increases gas-water interface (i.e. gas
The contact area of body and liquid), the sterilization effect of ozone is improved, also reduces energy consumption;
3) eccentric setting of inlet makes liquid have more great fluctuation process after retort is entered, add ozone bubbles with
The contact in hole, so as to the potential energy for expanding ozonization domain and when enhancing microbubbles rupture.
Brief description of the drawings
Fig. 1 is the front view of retort according to a preferred embodiment of the present invention
Fig. 2 is the A-A views of retort according to a preferred embodiment of the present invention
Fig. 3 is the stereogram of the retort of retort according to a preferred embodiment of the present invention
Fig. 4 is the partial view of ultrasonic variable amplitude bar according to a preferred embodiment of the present invention
Fig. 5 is schematic diagram according to a preferred embodiment of the present invention
Embodiment
Describe to be used to disclose the present invention below so that those skilled in the art can realize the present invention.It is excellent in describing below
Embodiment is selected to be only used as illustrating, it may occur to persons skilled in the art that other obvious modifications.
A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation as Figure 1-5 includes retort 1, multiple ultrasonic waves
Vibrating head 2, gas-liquid mixing pump 6 and ozone generator 7, the retort 1 include the inlet 4 and position positioned at the bottom of retort 1
Liquid outlet 5 in the bottom of retort 1, the delivery outlet of the gas-liquid mixing pump 6 connect with inlet 4, the liquid outlet 5 and outside
Water equipment connection.Liquid subject to sterilization flows into from the water inlet of the gas-liquid mixing pump 6, and the ozone generator 7 goes out
Gas port connects with gas-liquid mixing pump 6, ozone and liquid subject to sterilization mixing in the gas-liquid mixing pump 6, specifically, in gas-liquid
Ozone is divided into tiny bubble to be sufficiently mixed in liquid subject to sterilization by the impeller of mixing pump 6.Preferably, it is mixed smelly
The gas-water ratio of oxygen is 0.2~0.3mg/L, and the gas-liquid flow velocity of the inlet 4 is 1.5~1.7m/s, the tank body Gao Jing of retort 1
Than for 2.2~2.5:1, hydraulic detention time is 10~15 seconds, can further reduce energy consumption, and reaches preferably processing effect
Fruit.
The relative liquid of inlet 4 enters the eccentric axis setting in retort 1, so when liquid is from inlet 4
With bigger fluctuation and then more liquid can be made directly to be contacted with ultrasound wave vibrating bar 2 when entering retort 1, so as to
Reach more preferable sterilization effect.
The guide 8 extended along its axis direction is additionally provided with retort 1, the lower end of the guide 8 is fixed on reaction
The bottom of tank 1, the upper end of the guide 8 extend to the opening position at the close top of retort 1, and the liquid outlet 5 is in retort 1
Bottom on position and guide 8 position correspondence of the lower end on the bottom of retort 1, the liquid entered from inlet 4 is only
It can be entered from the upper end of guide 8 in guide 8, the lower end for then flowing through guide 8 is flowed out from liquid outlet 5.Set in the guide 8
It is equipped with the ultrasound wave vibrating bar 2 and then adds the chance that liquid subject to sterilization contacts with ultrasound wave vibrating bar 2, further improves
Sterilization effect.
Each ultrasound wave vibrating bar 2 include one end from the top of retort 1 be inserted into bottom ultrasonic transformer 22 and with change
Ultrasonic wave is delivered to retort by the ultrasonic transducer 21 of the top of width bar 22 connection, ultrasonic transducer 21 by ultrasonic transformer 22
In 1.The operation principle of the ultrasound wave vibrating bar 2 belongs to prior art, is no longer described in detail herein.The ultrasonic transducer
2115kHz~20kHz low-frequency sound wave.At least provided with the ultrasonic transformer 22 of a ultrasound wave vibrating bar 2 in the guide 8.
The surface of the ultrasonic transformer 22 is provided with multiple annular protrusions 23, the annular protrusion 23 add ultrasonic transformer 22 with
The contact area of liquid and then the effect that can further increase sterilizing.The power density of the ultrasonic transformer 22 (refers to unit area
The energy size that is radiated into water of ultrasonic transformer) be 1.5W/cm2。
The ultrasound wave vibrating bar 2 have it is multiple, by multiple ultrasound wave vibrating bars 2 can further improve sterilizing effect
Fruit.
General principle, principal character and the advantages of the present invention of the present invention has been shown and described above.The technology of the industry
For personnel it should be appreciated that the present invention is not limited to the above embodiments, that described in above-described embodiment and specification is the present invention
Principle, various changes and modifications of the present invention are possible without departing from the spirit and scope of the present invention, these change and
Improvement is both fallen within the range of claimed invention.The protection domain of application claims by appended claims and its
Equivalent defines.
Claims (7)
1. a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation, it is characterised in that including with inlet and liquid outlet
Retort, the ultrasound wave vibrating bar being inserted into retort, ozone generator and the internal gas-liquid with rotatable impeller
Mixing pump, the delivery outlet of the gas-liquid mixing pump connect with inlet, and the gas outlet of the ozone generator passes through pipeline and gas
Liquid mixing pump connects, and the liquid subject to sterilization connects also by pipeline with gas-liquid mixing pump.
A kind of 2. bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim 1, it is characterised in that it is described enter
Liquid mouth is arranged on the bottom of retort, and the liquid outlet is arranged on the bottom of retort, and guide is additionally provided with retort, institute
The lower end for stating guide is fixed on the bottom of retort and corresponding with liquid outlet, and upper end extends close to the top of retort, described
The opening for the upper end that liquid outlet passes through guide connects with inlet.
3. a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim 2, it is characterised in that described
At least provided with a ultrasound wave vibrating bar in guide.
A kind of 4. bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim 1, it is characterised in that it is described enter
Liquid mouth is set relative to the eccentric axis of retort.
5. a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim any one of 1-4, its feature exist
In the ultrasound wave vibrating bar includes being inserted into the ultrasonic transformer of bottom and the ultrasound being fixed at the top of ultrasonic transformer at the top of retort
Wave transducer, the surface that the ultrasonic transformer is located at the part in retort set multiple annular protrusions.
6. a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim 5, it is characterised in that described super
Acoustic vibration rod has multiple.
7. a kind of bactericidal unit based on ultrasound-enhanced ozone oxidation according to claim 1, it is characterised in that preferably
Ground, the retort in axial direction on height and diameter ratio be 2.2~2.5:1.
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CN201711063407.9A CN107601646A (en) | 2017-11-02 | 2017-11-02 | A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation |
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CN201711063407.9A CN107601646A (en) | 2017-11-02 | 2017-11-02 | A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112978849A (en) * | 2021-04-07 | 2021-06-18 | 宜兴帕克德环保技术有限公司 | Acousto-optic combined ultraviolet reactor |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030090362A (en) * | 2002-05-23 | 2003-11-28 | 한국과학기술원 | A combined process and device of ozone and sonication for water/wastewater treatment |
CN101274157A (en) * | 2006-12-31 | 2008-10-01 | 中国科学院过程工程研究所 | Cross current intrinsic cycle ultrasonic and microwave leaching reactor and leaching method thereof |
CN201279458Y (en) * | 2008-10-13 | 2009-07-29 | 陈元平 | High-power ultrasonic photochemistry treatment system |
JP2013180249A (en) * | 2012-03-02 | 2013-09-12 | Panasonic Corp | Water purification device |
CN105000627A (en) * | 2015-07-24 | 2015-10-28 | 中石化石油工程机械有限公司研究院 | Ozone oxidation reactor |
CN205500885U (en) * | 2016-03-28 | 2016-08-24 | 广东省环境科学研究院 | Ultrasonic wave ozone catalytic oxidation handles organic waste water's device |
CN207619090U (en) * | 2017-11-02 | 2018-07-17 | 上海李氏复大机电科技有限公司 | A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation |
-
2017
- 2017-11-02 CN CN201711063407.9A patent/CN107601646A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030090362A (en) * | 2002-05-23 | 2003-11-28 | 한국과학기술원 | A combined process and device of ozone and sonication for water/wastewater treatment |
CN101274157A (en) * | 2006-12-31 | 2008-10-01 | 中国科学院过程工程研究所 | Cross current intrinsic cycle ultrasonic and microwave leaching reactor and leaching method thereof |
CN201279458Y (en) * | 2008-10-13 | 2009-07-29 | 陈元平 | High-power ultrasonic photochemistry treatment system |
JP2013180249A (en) * | 2012-03-02 | 2013-09-12 | Panasonic Corp | Water purification device |
CN105000627A (en) * | 2015-07-24 | 2015-10-28 | 中石化石油工程机械有限公司研究院 | Ozone oxidation reactor |
CN205500885U (en) * | 2016-03-28 | 2016-08-24 | 广东省环境科学研究院 | Ultrasonic wave ozone catalytic oxidation handles organic waste water's device |
CN207619090U (en) * | 2017-11-02 | 2018-07-17 | 上海李氏复大机电科技有限公司 | A kind of bactericidal unit based on ultrasound-enhanced ozone oxidation |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112978849A (en) * | 2021-04-07 | 2021-06-18 | 宜兴帕克德环保技术有限公司 | Acousto-optic combined ultraviolet reactor |
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