CN106669524B - High-concentration ozone water integrated machine - Google Patents
High-concentration ozone water integrated machine Download PDFInfo
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- CN106669524B CN106669524B CN201710120350.5A CN201710120350A CN106669524B CN 106669524 B CN106669524 B CN 106669524B CN 201710120350 A CN201710120350 A CN 201710120350A CN 106669524 B CN106669524 B CN 106669524B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 97
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 238000006243 chemical reaction Methods 0.000 claims abstract description 65
- 238000000926 separation method Methods 0.000 claims abstract description 59
- 238000002156 mixing Methods 0.000 claims abstract description 43
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000006096 absorbing agent Substances 0.000 claims abstract description 9
- 239000005388 borosilicate glass Substances 0.000 claims description 19
- 239000010935 stainless steel Substances 0.000 claims description 14
- 229910001220 stainless steel Inorganic materials 0.000 claims description 14
- 239000003381 stabilizer Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000005192 partition Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- -1 polytetrafluoroethylene Polymers 0.000 claims description 3
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 3
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 3
- 238000009423 ventilation Methods 0.000 claims description 3
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 5
- 238000002360 preparation method Methods 0.000 abstract description 4
- 238000010521 absorption reaction Methods 0.000 abstract description 2
- 239000003814 drug Substances 0.000 abstract description 2
- 230000005611 electricity Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 33
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 210000003298 dental enamel Anatomy 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/18—Liquid substances or solutions comprising solids or dissolved gases
- A61L2/183—Ozone dissolved in a liquid
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The invention relates to the field of ozone water preparation, in particular to a high-concentration ozone water all-in-one machine. The all-in-one machine comprises a main control component, a high-concentration ozone generator (1), a low-pressure water source providing device (4), a gas-liquid mixing pump (5), a high-efficiency integrated reaction separation tank (6), a high-pressure pump (12), a tail gas absorber (19) and a high-concentration ozone water collecting device (21); also comprises a jet flow mixer (13) and a multi-stage efficient mixer (14). The integrated machine is additionally provided with a secondary ozone absorption pressurization mixing system, so that the utilization rate of ozone gas is increased, and the ozone gas can be dissolved in water to a greater extent; simultaneously, the device has the characteristics of one-key start and stop, water and electricity protection, low tail gas treatment difficulty, convenient operation and capability of moving at any time, and can realize diversified control. The high-concentration ozone water produced by the integrated machine can reach the disinfection standard in the field of medicine.
Description
Technical Field
The invention relates to the field of ozone water preparation, in particular to a high-concentration ozone water all-in-one machine.
Background
In the prior art, an apparatus for preparing ozone water is mainly composed of an ozone gas generator main body and a mixing apparatus. The ozone gas generator body is made of a high dielectric constant material and can be divided into three general types: glass, enamel and ceramics are also divided into different generators according to the material and the process of the materials of the glass, the enamel and the ceramics. The more delicate and fine the material used, the higher the concentration of ozone produced. The positive electrode material of the ozone gas generator comprises carbon steel, stainless steel, aluminum alloy, graphite and the like. The gas source of the ozone gas generator is used for providing gas for the ozone gas generator, the oxygen content in the gas source is determined by the type of the gas source, wherein when the gas source is air, the oxygen concentration is lowest; the gas source uses an oxygen generator to provide oxygen, and the oxygen is secondarily contained; when the gas source uses pure oxygen, the oxygen concentration is highest.
The mixing mode of the mixing equipment is mainly a jet flow mixing mode and a gas-liquid mixing pump mixing mode.
The existing ozone water preparation equipment is designed in a machine body separation mode, and the number of pipelines and electric control points is too many, so that the operation is inconvenient. The mixing mode used in the ozone water preparation equipment is gas-liquid mixing pump mixing or simple stirring and pressurizing mixing. The ozone water produced by adopting the two mixing modes has low concentration, can only carry out simple sterilization and disinfection, has slightly insufficient concentration when the surface of an object is sterilized and disinfected, and particularly can not reach the required concentration when medicinal materials are sterilized and disinfected. Meanwhile, the un-mixed ozone gas is discharged or decomposed, and the part of ozone is prepared by consuming a large amount of electric power, so that resources are seriously wasted, and the concept of environmental protection is not met.
Disclosure of Invention
The invention aims to provide the high-concentration ozone water all-in-one machine which is simple and convenient to operate, is green and environment-friendly and is used for preparing the ozone water with the concentration meeting the sterilization requirement.
The scheme adopted by the invention for solving the technical problem is as follows:
the high-concentration ozone water all-in-one machine comprises a main control component, a high-concentration ozone generator 1, a low-pressure water source providing device 4, a gas-liquid mixing pump 5, a high-efficiency integrated reaction separation tank 6, a high-pressure pump 12, a tail gas absorber 19 and a high-concentration ozone water collecting device 21, and further comprises a jet flow mixer 13 and a multi-stage high-efficiency mixer 14.
The high-concentration ozone generator 1 is internally provided with a positive reaction electrode and a negative reaction electrode, the positive electrode is an ultrathin high borosilicate glass tube 24, and the surface of the ultrathin high borosilicate glass tube 24 is coated with a conductive layer of graphene conductive coating; the cathode is a precision stainless steel tube 23; the precision stainless steel tube 23 penetrates through the ultrathin high borosilicate glass tube 24, and a gas channel is formed between the precision stainless steel tube and the ultrathin high borosilicate glass tube; and air ventilation gaskets 25 are fixedly arranged at two ends of the ultrathin high borosilicate glass tube 24.
The inlet of the gas-liquid mixing pump 5 is respectively communicated with the high-concentration ozone generator 1 and the low-pressure water source supply device 4 through pipelines.
The inside of the high efficiency integrated reaction separation tank 6 is partitioned into a first chamber and a second chamber by a partition 22.
A spherical flow damper 7 and a flow stabilizer 8 are arranged on the side wall in the first chamber of the high-efficiency integrated reaction separation tank 6; a water inlet of a first chamber of the high-efficiency integrated reaction separation tank 6 is communicated with an outlet of the gas-liquid mixing pump 5 through a pipeline, and the spherical flow damper 7 is arranged below the water inlet; the flow stabilizer 8 is arranged below the spherical flow damper 7.
An impact mixer bracket 16 and an impact mixer 15 are arranged in the second chamber of the high-efficiency integrated reaction separation tank 6; the impact mixer support 16 is fixed on the inner wall of the top end of the second chamber of the high-efficiency integrated reaction separation tank 6, and the impact mixer 15 is fixedly arranged on the impact mixer support 16.
The bottom of the second chamber of the high-efficiency integrated reaction separation tank 6 is communicated with a high-concentration ozone water collecting device 21 through a pipeline.
The inlet of the high-pressure pump 12 is communicated with the bottom of the first chamber of the high-efficiency integrated reaction separation tank 6 through a pipeline.
A first-stage automatic exhaust valve 11 is arranged on the wall of the first chamber of the high-efficiency integrated reaction separation tank 6; the inlet of the jet mixer 13 is respectively communicated with the first-stage automatic exhaust valve 11 and the outlet of the high-pressure pump 12 through pipelines.
The inlet of the multi-stage high-efficiency mixer 14 is communicated with the outlet of the jet flow mixer 13, and the outlet of the multi-stage high-efficiency mixer 14 is communicated with an impact mixer 15 in the second chamber of the high-efficiency integrated reaction separation tank 6 through a pipeline.
A secondary automatic exhaust valve 18 is arranged on the outer tank wall of the second chamber of the high-efficiency integrated reaction separation tank 6; the secondary automatic exhaust valve 18 is connected with a tail gas absorber 19.
An ozone electromagnetic valve 2 is arranged on a pipeline between the high-concentration ozone generator 1 and the mixing pump 5.
A water flow switch 3 is arranged on a pipeline which is communicated with the first chamber of the high-efficiency integrated reaction tank 6 by the gas-liquid mixing pump 5.
The first chamber of the high-efficiency integrated reaction separation tank 6 is provided with a primary pressure sensor 9.
A first-stage middle electric valve 10 is arranged on a pipeline between the first chamber of the high-efficiency integrated reaction separation tank 6 and the high-pressure pump 12.
A second-stage pressure sensor 17 is arranged in the second chamber of the high-efficiency integrated reaction separation tank 6.
A second-stage water production electric valve 20 is arranged on a pipeline between the second chamber of the high-efficiency integrated reaction separation tank 6 and the high-concentration ozone water collecting device 21.
The high-concentration ozone generator 1 is electrically connected with the main control component.
The main control part is respectively and electrically connected with the ozone electromagnetic valve 2, the water flow switch 3, the primary pressure sensor 9, the primary middle electric valve 10, the primary automatic exhaust valve 11, the secondary pressure sensor 17, the secondary automatic exhaust valve 18 and the secondary water production electric valve 20.
The distance between the ultrathin high borosilicate glass tube 24 and the precision stainless steel tube 23 is 1.5mm.
The material of the fixed ventilation gasket 25 is polytetrafluoroethylene.
The flow stabilizer 8 has a working cross-section identical to the cross-section of the first chamber.
The direction of the partition plate 22 for dividing the high-efficiency integrated reaction separation tank 6 is a vertical direction.
The invention has the beneficial effects that:
1) The high-concentration ozone water generated by the high-concentration ozone water all-in-one machine can improve the disinfection level of the ozone water on the surface of an object and can reach the disinfection standard in the field of medicine;
2) A secondary ozone absorption pressurization mixing system is added, so that the utilization rate of ozone gas is increased, and the ozone gas can be dissolved in water to a greater extent;
3) The ozone gas emission is reduced, the tail gas treatment difficulty is reduced, and the environment is not polluted;
4) The integrated machine has the advantages of one-key start-stop and water-electricity protection, convenient operation, capability of being moved at any time and realization of diversified control.
Drawings
FIG. 1 is a schematic structural diagram of the high concentration ozone water all-in-one machine of the present invention;
fig. 2 is a schematic diagram of the positive and negative electrodes of the high concentration ozone generator 1 of the high concentration ozone water all-in-one machine of the present invention.
Wherein the reference numerals are:
1. high concentration ozone generator 2 ozone electromagnetic valve
3. Water flow switch 4 low-pressure water source providing device
5. High-efficiency integrated reaction separation tank of gas-liquid mixing pump 6
7. Spherical flow damper 8 flow stabilizer
9. Primary pressure sensor 10 primary middle electric valve
11. 12 high-pressure pump with one-stage automatic exhaust valve
13. Jet mixer 14 multistage high-efficiency mixer
15. Impingement mixer 16 impingement mixer holder
17. Two-stage pressure sensor 18 two-stage automatic exhaust valve
19. Tail gas absorber 20 two-stage water production electric valve
21. High concentration ozone water collecting device 22 baffle
23. Precise stainless steel 24 ultrathin high borosilicate glass tube
25. Fixed ventilating cushion ring
Detailed Description
The invention will be further explained with reference to the drawings.
As shown in fig. 1, the high concentration ozone water all-in-one machine of the present invention comprises a main control unit, a high concentration ozone generator 1, a low pressure water source providing device 4, a gas-liquid mixing pump 5, a high efficiency integrated reaction separation tank 6, a high pressure pump 12, a jet mixer 13, a multistage high efficiency mixer 14, a tail gas absorber 19 and a high concentration ozone water collecting device 21, wherein:
as shown in fig. 2, the high concentration ozone generator 1 is provided with a positive and a negative reaction electrode, the positive electrode is an ultra-thin borosilicate glass tube 24, and the surface of the ultra-thin borosilicate glass tube 24 is coated with a conductive layer of graphene conductive coating; the negative electrode is a precision stainless steel tube 23. The precision stainless steel tube 23 penetrates through the ultra-thin high borosilicate glass tube 24, and a gas channel is formed between the precision stainless steel tube and the ultra-thin high borosilicate glass tube. And two ends of the ultrathin high borosilicate glass tube 24 are provided with fixed air-permeable cushion rings 25, and the materials of the fixed air-permeable cushion rings 25 are polytetrafluoroethylene. Preferably, the distance between the ultra-thin borosilicate glass tube 24 and the precision stainless steel tube 23 is 1.5mm.
The inlet of the gas-liquid mixing pump 5 is respectively communicated with the high-concentration ozone generator 1 and the low-pressure water source supply device 4 through pipelines.
The inside of the high-efficiency integrated reaction separation tank 6 is divided into a first chamber and a second chamber by a partition plate 22; preferably, the direction in which the partition plate 22 partitions the high-efficiency integrated reaction separation tank 6 is a vertical direction.
The side wall in the first chamber of the high-efficiency integrated reaction separation tank 6 is provided with a spherical flow damper 7 and a flow stabilizer 8 through bolts. A water inlet of a first chamber of the high-efficiency integrated reaction separation tank 6 is communicated with an outlet of the gas-liquid mixing pump 5 through a pipeline, and the spherical flow damper 7 is arranged below the water inlet; the flow stabilizer 8 is arranged below the spherical flow damper 7 and has a working section the same as the cross section of the first chamber.
An impact mixer bracket 16 and an impact mixer 15 are arranged in the second chamber of the high-efficiency integrated reaction separation tank 6; the impact mixer support 16 is fixed on the inner wall of the top end of the second chamber of the high-efficiency integrated reaction separation tank 6 through bolts, and the impact mixer 15 is fixedly arranged on the impact mixer support 16 through bolts.
The bottom of the second chamber of the high-efficiency integrated reaction separation tank 6 is communicated with a high-concentration ozone water collecting device 21 through a pipeline.
The inlet of the high-pressure pump 12 is communicated with the bottom of the first chamber of the high-efficiency integrated reaction separation tank 6 through a pipeline.
The first chamber of the high-efficiency integrated reaction separation tank 6 is provided with a first-stage automatic exhaust valve 11 on the wall. The inlet of the jet mixer 13 is respectively communicated with the first-stage automatic exhaust valve 11 and the outlet of the high-pressure pump 12 through pipelines.
The inlet of the multi-stage high-efficiency mixer 14 is communicated with the outlet of the jet flow mixer 13, and the outlet of the multi-stage high-efficiency mixer 14 is communicated with the impact mixer 15 in the second chamber of the high-efficiency integrated reaction separation tank 6 through a pipeline.
The second-stage automatic exhaust valve 18 is arranged on the wall of the second chamber of the high-efficiency integrated reaction separation tank 6. The secondary automatic exhaust valve 18 is connected with a tail gas absorber 19.
An ozone electromagnetic valve 2 is arranged on a pipeline between the high-concentration ozone generator 1 and the mixing pump 5.
A water flow switch 3 is arranged on a pipeline which is communicated with the first chamber of the high-efficiency integrated reaction tank 6 by the gas-liquid mixing pump 5.
The first chamber of the high-efficiency integrated reaction separation tank 6 is provided with a primary pressure sensor 9.
A first-stage middle electric valve 10 is arranged on a pipeline between the first chamber of the high-efficiency integrated reaction separation tank 6 and the high-pressure pump 12.
A second-stage pressure sensor 17 is arranged in the second chamber of the high-efficiency integrated reaction separation tank 6.
A second-stage water production electric valve 20 is arranged on a pipeline between the second chamber of the high-efficiency integrated reaction separation tank 6 and the high-concentration ozone water collecting device 21.
The high-concentration ozone generator 1 is electrically connected with the main control unit.
The main control part is respectively and electrically connected with the ozone electromagnetic valve 2, the water flow switch 3, the primary pressure sensor 9, the primary middle electric valve 10, the primary automatic exhaust valve 11, the secondary pressure sensor 17, the secondary automatic exhaust valve 18 and the secondary water production electric valve 20.
The working process of the invention is as follows:
the gas-liquid mixing pump 5 is started, the water source provided by the low-pressure water source providing device 4 flows through the gas-liquid mixing pump 5, when the water source passes through the water flow switch 3, the water flow switch 3 senses that water flow continuously passes through and sends a signal to the main control unit, the main control unit controls the high-concentration ozone generator 1 to start to prepare ozone gas after receiving the signal, and meanwhile, the ozone electromagnetic valve 2 is controlled to be opened. The gas-liquid mixing pump 5 pumps the high-concentration ozone gas generated in the high-concentration ozone generator 1 to mix it with water in the gas-liquid mixing pump 5 for the first time.
The ozone water after the first mixing enters a first chamber of a high-efficiency integrated reaction separation tank 6, and after slowly flowing through a spherical flow damper 7, primary pressurization is carried out in the first chamber. The pressure is set by the master control unit. When the pressure in the first chamber of the high-efficiency integrated reaction separation tank 6 reaches a set value, the primary pressure sensor 9 transmits a signal to the primary intermediate electric valve 10 through the main control unit to open the primary intermediate electric valve.
Starting the high-pressure pump 12, stabilizing the flow of the ozone water after the primary pressurization by the flow stabilizer 8, pumping the ozone water into the jet flow mixer 13 by the high-pressure pump 12 at a high speed, simultaneously sucking the residual ozone gas in the first chamber of the high-efficiency integrated reaction separation tank 6 into the jet flow mixer 13 through the primary automatic exhaust valve 11, and respectively mixing the ozone water and the residual ozone gas into the jet flow mixer 13 through the high-pressure pump 12 and the primary automatic exhaust valve 11 for secondary mixing. The ozone water after the secondary mixing is cut and mixed evenly by a multi-stage high-efficiency mixer 14, enters a second chamber of a high-efficiency integrated reaction separation tank 6 for secondary pressurization, and is sprayed to an impact mixer 15 in a spraying mode.
After the ozone water is impacted, part of ozone gas dissolved in the water escapes again. During the secondary pressurization in the second chamber of the highly efficient integrated reaction tank 6, the escaping ozone gas is re-dissolved in the falling ozone water.
Through twice mixing and pressurized dissolving, ozone water in the high-efficiency integrated reaction separation tank 6 is supersaturated in ozone and oxygen solubility, and in the twice mixing process, the gas-liquid mixing pump 5 and the high-pressure pump 12 enable ozone in water to exist in ozone water in a micron or even nanometer level state under the action of cutting water force, so that the ozone concentration is increased, and the attenuation time of ozone in water is reduced.
The pressure in the second chamber of the high efficiency integrated reaction separation tank 6 is set by the main control unit. When the pressure in the second chamber of the high-efficiency integrated reaction separation tank 6 reaches a set value, the secondary pressure sensor 17 transmits a signal to the secondary water production electric valve 20 to open the secondary water production electric valve, and the high-concentration ozone water can flow out and be directly used or used for preparing ozone water products. The residual gas in the second chamber can enter a tail gas absorber 19 through a secondary automatic exhaust valve 18 to realize tail gas recovery.
Preferably, the activation time of the high-pressure pump 12 is: 15 seconds after the start of the gas-liquid mixing pump 5.
If the water flow switch 3 does not pass water or the water flow is interrupted after the gas-liquid mixing pump 5 is started, the signal given to the main control unit by the water flow switch 3 is interrupted. At this point the master control unit will shut down all devices in operation.
The water source is a stable low-pressure sufficient water source, no impurities and no bubbles exist in the water source, and the water temperature is normal temperature or lower than the normal temperature.
Claims (3)
1. High concentration ozone water all-in-one, including main control unit, high concentration ozone generator (1), low pressure water source provide device (4), gas-liquid mixing pump (5), high-efficient integrated reaction-separation jar (6), high-pressure pump (12), tail gas absorber (19) and high concentration ozone water collection device (21), its characterized in that: also comprises a jet flow mixer (13) and a multi-stage efficient mixer (14); wherein,
the high-concentration ozone generator (1) is internally provided with a positive reaction electrode and a negative reaction electrode, the positive electrode is an ultrathin high borosilicate glass tube (24), and the surface of the ultrathin high borosilicate glass tube (24) is coated with a conductive layer of graphene conductive coating; the cathode is a precision stainless steel tube (23); the precision stainless steel pipe (23) penetrates through the ultrathin high borosilicate glass pipe (24), and a gas channel is formed between the precision stainless steel pipe and the ultrathin high borosilicate glass pipe; two ends of the ultrathin high borosilicate glass tube (24) are provided with fixed ventilating gaskets (25);
the inlet of the gas-liquid mixing pump (5) is respectively communicated with the high-concentration ozone generator (1) and the low-pressure water source supply device (4) through pipelines;
the inside of the high-efficiency integrated reaction separation tank (6) is divided into a first chamber and a second chamber by a partition plate (22);
a spherical flow damper (7) and a flow stabilizer (8) are arranged on the side wall in a first chamber of the high-efficiency integrated reaction separation tank (6); a water inlet of a first chamber of the high-efficiency integrated reaction separation tank (6) is communicated with an outlet of the gas-liquid mixing pump (5) through a pipeline, and the spherical flow damper (7) is arranged below the water inlet; the flow stabilizer (8) is arranged below the spherical flow damper (7);
an impact mixer bracket (16) and an impact mixer (15) are arranged in the second chamber of the high-efficiency integrated reaction separation tank (6); the impact mixer bracket (16) is fixed on the inner wall of the top end of the second chamber of the high-efficiency integrated reaction separation tank (6), and the impact mixer (15) is installed and fixed on the impact mixer bracket (16);
the bottom of the second chamber of the high-efficiency integrated reaction separation tank (6) is communicated with a high-concentration ozone water collecting device (21) through a pipeline;
the inlet of the high-pressure pump (12) is communicated with the bottom of the first chamber of the high-efficiency integrated reaction separation tank (6) through a pipeline;
a first-stage automatic exhaust valve (11) is arranged on the outer tank wall of the first chamber of the high-efficiency integrated reaction separation tank (6); the inlet of the jet flow mixer (13) is respectively communicated with the first-stage automatic exhaust valve (11) and the outlet of the high-pressure pump (12) through pipelines;
the inlet of the multi-stage high-efficiency mixer (14) is communicated with the outlet of the jet flow mixer (13), and the outlet of the multi-stage high-efficiency mixer (14) is communicated with an impact mixer (15) in a second chamber of the high-efficiency integrated reaction separation tank (6) through a pipeline;
a secondary automatic exhaust valve (18) is arranged on the outer tank wall of the second chamber of the high-efficiency integrated reaction separation tank (6); the secondary automatic exhaust valve (18) is connected with a tail gas absorber (19);
an ozone electromagnetic valve (2) is arranged on a pipeline between the high-concentration ozone generator (1) and the gas-liquid mixing pump (5);
a water flow switch (3) is arranged on a pipeline which is communicated with the first chamber of the high-efficiency integrated reaction separation tank (6) by the gas-liquid mixing pump (5);
a first chamber of the high-efficiency integrated reaction separation tank (6) is provided with a first-stage pressure sensor (9);
a first-stage middle electric valve (10) is arranged on a pipeline between the first chamber of the high-efficiency integrated reaction separation tank (6) and the high-pressure pump (12);
a second-stage pressure sensor (17) is arranged in a second chamber of the high-efficiency integrated reaction separation tank (6);
a second-stage water production electric valve (20) is arranged on a pipeline between the second chamber of the high-efficiency integrated reaction separation tank (6) and the high-concentration ozone water collecting device (21);
the high-concentration ozone generator (1) is electrically connected with the main control unit;
the main control part is respectively and electrically connected with the ozone electromagnetic valve (2), the water flow switch (3), the primary pressure sensor (9), the primary middle electric valve (10), the primary automatic exhaust valve (11), the secondary pressure sensor (17), the secondary automatic exhaust valve (18) and the secondary water production electric valve (20);
the fixed ventilation gasket (25) is made of polytetrafluoroethylene;
the flow stabilizer (8) has a working section identical to the cross section of the first chamber.
2. The high concentration ozonated water all-in-one of claim 1, wherein: the distance between the ultrathin high borosilicate glass tube (24) and the precise stainless steel tube (23) is 1.5mm.
3. The high concentration ozonated water all-in-one of claim 1 or 2, wherein: the direction of the partition plate (22) for separating the high-efficiency integrated reaction separation tank (6) is vertical.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710120350.5A CN106669524B (en) | 2017-03-02 | 2017-03-02 | High-concentration ozone water integrated machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710120350.5A CN106669524B (en) | 2017-03-02 | 2017-03-02 | High-concentration ozone water integrated machine |
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| CN106669524A CN106669524A (en) | 2017-05-17 |
| CN106669524B true CN106669524B (en) | 2023-04-07 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108745013B (en) * | 2018-07-19 | 2023-11-10 | 苏州方舟环保科技有限公司 | High-concentration ozone water manufacturing equipment for sterilization and disinfection |
| CN110237729A (en) * | 2019-06-26 | 2019-09-17 | 中实泰广(北京)环保科技有限公司 | The saturation dissolver of the saturation dissolving method and ozone and water of ozone and water |
| CN112923619A (en) * | 2021-03-19 | 2021-06-08 | 北京宜清源科技有限公司 | Method and equipment for industrially, rapidly and efficiently preparing ozone ice |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0372993A (en) * | 1989-08-10 | 1991-03-28 | Ishikawajima Harima Heavy Ind Co Ltd | Ozone manufacturing device |
| CN1583597A (en) * | 2004-06-15 | 2005-02-23 | 朱方俊 | Circulating water apparatus treated by high-concentration ozone |
| CN203451859U (en) * | 2013-08-08 | 2014-02-26 | 天津斯巴克瑞科技发展有限公司 | Environment-friendly washing intensifier |
| CN106268386A (en) * | 2016-09-18 | 2017-01-04 | 中国科学院上海高等研究院 | A kind of continuous way prepares the method and device of high-concentration ozone water |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9068149B2 (en) * | 2007-03-14 | 2015-06-30 | Food Safety Technology, Llc | Ozone cleaning system |
| CN206549571U (en) * | 2017-03-02 | 2017-10-13 | 北京博纳源环保科技有限公司 | High-concentration ozone water all-in-one |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0372993A (en) * | 1989-08-10 | 1991-03-28 | Ishikawajima Harima Heavy Ind Co Ltd | Ozone manufacturing device |
| CN1583597A (en) * | 2004-06-15 | 2005-02-23 | 朱方俊 | Circulating water apparatus treated by high-concentration ozone |
| CN203451859U (en) * | 2013-08-08 | 2014-02-26 | 天津斯巴克瑞科技发展有限公司 | Environment-friendly washing intensifier |
| CN106268386A (en) * | 2016-09-18 | 2017-01-04 | 中国科学院上海高等研究院 | A kind of continuous way prepares the method and device of high-concentration ozone water |
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