CN106334490B - Energy storage type laminating mixing device and method for ozone water - Google Patents
Energy storage type laminating mixing device and method for ozone water Download PDFInfo
- Publication number
- CN106334490B CN106334490B CN201610877151.4A CN201610877151A CN106334490B CN 106334490 B CN106334490 B CN 106334490B CN 201610877151 A CN201610877151 A CN 201610877151A CN 106334490 B CN106334490 B CN 106334490B
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- water
- mixer
- pressure
- ozone
- energy storage
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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
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
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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
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
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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
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23761—Aerating, i.e. introducing oxygen containing gas in liquids
- B01F23/237613—Ozone
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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
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7179—Feed mechanisms characterised by the means for feeding the components to the mixer using sprayers, nozzles or jets
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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
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
Abstract
An energy-storage type membrane-covering mixing device for ozone water and a mode thereof are characterized in that a primary gas-water mixer, a secondary membrane-covering mixer and a tertiary differential pressure flow mixer are installed in an energy-storage container body, the primary gas-water mixer is connected with a pressure water inlet interface, a diffusion type jet nozzle is arranged in the pressure water inlet interface, an ozone input control valve is installed on the inlet side of the primary gas-water mixer, a multi-point membrane-covering mixing hole is formed in the tail end of the primary gas-water mixer and communicated with the secondary membrane-covering mixer, a vortex group is arranged in the secondary membrane-covering mixer, the output end of the secondary membrane-covering mixer is connected to the inner wall of the energy-storage container body, namely the inlet end of the tertiary differential pressure flow mixer, and a membrane-covering mixed water output control valve is installed in the middle of the energy-storage container body.
Description
Technical Field
The invention relates to a mixing device of ozone water, in particular to an energy storage type film coating mixing device of ozone water and a mode thereof.
Background
At present, most of the ozone water mixing at home and abroad is Venturi gas-water mixing, pump mixing and the like, and a few manufacturers use a composite mode for mixing. Because the Venturi jet flow mode mixing, the pump extrusion mode mixing and the composite mode mixing can not generate dense bubble groups, ozone and water can not be mixed in a laminating way, and the ozone on the water surface is separated from the water surface and is diffused in the air, so that secondary pollution to the environment within a certain time is caused, and precious energy is wasted.
The Chinese patent discloses a cascade gas-water mixing device (01238243.4), which comprises a venturi jet mixer and an ozone contact separation chamber, wherein the water outlet of the venturi jet mixer is communicated with the water inlet of the ozone contact separation chamber to form a group of mixing mechanisms, more than two groups of mixing mechanisms form the device, the gas circuits of each group of gas-water mixing mechanisms are connected in series, and the water circuits of each group of gas-water mixing mechanisms are connected in parallel.
Chinese patent has disclosed a aqueous vapor mixing arrangement (201320068514.1), including connecting gradually ejector, centrifugal pump and shunt, the ejector is connected ozone generator and is inhaled ozone, is connected with a blender between centrifugal pump and the shunt, and the blender is the body that both ends switched on, is equipped with wavy passageway in the body, the aperture of passageway is less than the aperture of body, flange joint has the guide plate between centrifugal pump and the blender, is equipped with a through-hole on the guide plate, and the through-hole aperture is less than the aperture of body. The flow divider is a reducing pipe and is provided with a wave-shaped water outlet, the water outlet section is gradually reduced, the flow velocity is increased, high-concentration ozone water can be obtained, the sterilization and disinfection effects are strong, the atmospheric pollution is reduced, and the energy-saving and environment-friendly effects are achieved.
Disclosure of Invention
The invention aims to solve the serious defects that the existing ozone and water cannot be mixed in a film covering mode, and the ozone on the water surface is separated from the water surface and is emitted into the air, so that secondary pollution to the environment and energy waste are caused within a certain time, and provides an energy storage type film covering mixing device and method for ozone water.
In order to achieve the purpose, the invention adopts the following solution: the utility model provides an energy storage formula tectorial membrane mixing arrangement of ozone water, install elementary gas-water mixer, second grade tectorial membrane blender and tertiary differential pressure flow blender in the energy storage container body, elementary gas-water mixer connects the pressure water interface of intaking, there is diffusion formula efflux nozzle in the pressure water interface of intaking, ozone input control valve is equipped with to elementary gas-water mixer inlet side, it has multipoint mode tectorial membrane mixing hole to open on the elementary gas-water mixer tip, multipoint mode tectorial membrane mixing hole communicates with each other with second grade tectorial membrane blender, have the vortex group in the second grade tectorial membrane blender, second grade tectorial membrane blender output to the bottom chamber of the energy storage container body, the entrance point of tertiary differential pressure flow blender is in the bottom chamber of the energy storage container body, the middle part installation tectorial membrane mixed water output control valve of the energy storage container body.
When pressure water enters a pressure water inlet interface, a diffusion jet nozzle in the pressure water inlet interface sprays the pressure water in a primary gas-water mixer in a diffusion mode to generate negative pressure with pressure difference corresponding to the pressure water, an ozone input control valve is opened, ozone enters the primary gas-water mixer to be primarily mixed with the pressure water, primary bubbles and the pressure water after primary mixing enter a multi-point type film coating mixing hole to be extruded, bubble group mixed water is formed after bubble fission and enters a secondary film coating mixer, the bubble group uniformly enters a tertiary pressure difference flow mixer under the reverse diffusion and extrusion action of a vortex sheet group in the secondary film coating mixer, the tertiary pressure difference flow mixer gradually changes the volume and rises to the pressure equal to the pressure peak value of the pressure water under the compression characteristic of an energy storage container body to uniformly coat the ozone and the bubbles, the obtained ozone water is output by a film-coated mixed water output control valve.
Compared with the prior art, the energy storage type laminating mixing device and the mode thereof for ozone water are provided. Has the following positive effects: the ozone generator can form a bubble group with dense film covering, so that ozone and water are deeply mixed in the bubble film, and the retention time of the ozone in the bubble film is stabilized.
Drawings
Fig. 1 is a schematic structural diagram of the present embodiment.
In the figure: 1. the device comprises a pressure water inlet interface, 2, a diffusion type jet nozzle, 3, a primary gas-water mixer, 4, an ozone input control valve, 5, a multi-point type film coating mixing hole, 6, a secondary film coating mixer, 7, a three-level differential pressure flow mixer, 8, an energy storage container body, 9 and a film coating mixed water output control valve.
Detailed Description
The present invention will be described with reference to the following embodiments and accompanying drawings.
Referring to fig. 1, an energy storage type membrane mixing device for ozone water, a primary gas-water mixer 3, a secondary membrane mixer 6 and a tertiary differential pressure flow mixer 7 are installed in an energy storage container body 8, the primary gas-water mixer 3 is connected with a pressure water inlet interface 1, a diffusion type jet nozzle 2 is arranged in the pressure water inlet interface 1, an ozone input control valve 4 is installed on the inlet side of the primary gas-water mixer 3, a multi-point membrane covering mixing hole 5 is formed in the tail end of the primary gas-water mixer 3, the multi-point membrane covering mixing hole 5 is communicated with the secondary membrane mixer 6, a vortex group is arranged in the secondary membrane mixer 6, the output end of the secondary membrane covering mixer 6 is connected to the bottom cavity of the energy storage container body 8, the inlet end of the tertiary differential pressure flow mixer 7 is located in the bottom cavity of the energy storage container body 8, and a membrane covering mixed water output control valve 9 is installed in the middle of the energy storage container body 8.
Referring to fig. 1, an ozone water mixing method using the above ozone water energy storage type coating mixing device, when pressure water enters a pressure water inlet port 1, a diffusion type jet nozzle 2 in the pressure water inlet port 1 sprays the pressure water in a diffusion manner in a primary gas-water mixer 3 to generate negative pressure corresponding to pressure water pressure difference, ozone input control valve 4 is opened, ozone enters the primary gas-water mixer 3 to be primarily mixed with the pressure water, primary bubbles and the pressure water after primary mixing enter a multi-point type coating mixing hole 5 to be extruded, bubble group mixed water formed after bubble fission enters a secondary coating mixer 6, the bubble group mixed water uniformly enters a tertiary pressure difference flow mixer 7 under the reverse diffusion extrusion action of a vortex sheet set in the secondary coating mixer 6, and the volume of a container body of the tertiary pressure difference flow mixer 7 gradually changes the pressure and rises to be equal to the pressure water peak value under the spatial compression characteristic of an energy storage 8, so that the ozone and the bubbles are obtained The uniform coating is mixed, and the obtained ozone water is output by a coating mixed water output control valve 9.
Claims (1)
1. The utility model provides an energy storage formula tectorial membrane hybrid mode of ozone water, install elementary gas-water mixer in the energy storage container body, second grade tectorial membrane mixer and tertiary differential pressure stream blender, elementary gas-water mixer connects the pressure water interface of intaking, there is diffusion formula efflux nozzle in the pressure water interface of intaking, ozone input control valve is equipped with to elementary gas-water mixer inlet side, it has multipoint mode tectorial membrane mixing hole to open on the elementary gas-water mixer tip, multipoint mode tectorial membrane mixing hole communicates with each other with second grade tectorial membrane mixer, have the vortex group in the second grade tectorial membrane mixer, second grade tectorial membrane mixer output to the bottom chamber of the energy storage container body, the entrance point of tertiary differential pressure stream blender is in the bottom chamber of the energy storage container body, the mid-mounting tectorial membrane mixed water output control valve of the energy storage container body, characterized by: when pressure water enters a pressure water inlet interface, a diffusion jet nozzle in the pressure water inlet interface sprays the pressure water in a primary gas-water mixer in a diffusion mode to generate negative pressure with pressure difference corresponding to the pressure water, so that an ozone input control valve is opened, ozone enters the primary gas-water mixer to be primarily mixed with the pressure water, primary bubbles and the pressure water after primary mixing enter a multi-point type film coating mixing hole to be extruded, bubble group mixed water is formed after the bubbles are cracked and enters a secondary film coating mixer, under the action of back diffusion and extrusion of a vortex sheet set in the secondary coating mixer, bubble groups uniformly enter the tertiary differential pressure flow mixer, the volume of the tertiary differential pressure flow mixer gradually changes under the space compression characteristic of an energy storage container, the pressure rises to be equal to the pressure water peak value in the compression process, ozone and bubbles are uniformly coated and mixed, and the obtained ozone water is output by a coating mixed water output control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610877151.4A CN106334490B (en) | 2016-09-29 | 2016-09-29 | Energy storage type laminating mixing device and method for ozone water |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610877151.4A CN106334490B (en) | 2016-09-29 | 2016-09-29 | Energy storage type laminating mixing device and method for ozone water |
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| Publication Number | Publication Date |
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| CN106334490A CN106334490A (en) | 2017-01-18 |
| CN106334490B true CN106334490B (en) | 2022-08-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610877151.4A Active CN106334490B (en) | 2016-09-29 | 2016-09-29 | Energy storage type laminating mixing device and method for ozone water |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108187517A (en) * | 2018-02-26 | 2018-06-22 | 浙江览锐智能科技有限公司 | A kind of continuous overlay film mixing arrangement of Ozone Water and its mode |
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| JPH03127657A (en) * | 1989-10-11 | 1991-05-30 | Hashimoto Denki Co Ltd | Mixer in two-pack pressure mixing sprayer for adhesive or the like |
| CN2334753Y (en) * | 1997-12-01 | 1999-08-25 | 侯传绪 | Ozone water generator |
| CN2347966Y (en) * | 1998-06-18 | 1999-11-10 | 史腊求 | Energy-saving sewage aerator |
| EP1329254A1 (en) * | 2001-11-23 | 2003-07-23 | Hermann Böck | Device and process for mixing of liquid, viscous and/or pourable media |
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| CN101832154A (en) * | 2009-03-11 | 2010-09-15 | 中国科学院工程热物理研究所 | Method for cooling air film of turbine blade of aircraft engine |
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| CN202017516U (en) * | 2011-03-21 | 2011-10-26 | 西安西科煤矿安全通风防灭火研究所有限公司 | Fireproof extinguishing foam generator for mining |
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| GB2406293B (en) * | 2003-09-29 | 2008-05-14 | Dynamic Proc Solutions Plc | Apparatus for enhancing solubility |
| CA2561539C (en) * | 2006-09-28 | 2016-11-08 | Hydro Processing & Mining Ltd. | Apparatus and method for efficient particle to gas bubble attachment in a slurry |
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Patent Citations (13)
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|---|---|---|---|---|
| JPH03127657A (en) * | 1989-10-11 | 1991-05-30 | Hashimoto Denki Co Ltd | Mixer in two-pack pressure mixing sprayer for adhesive or the like |
| CN2334753Y (en) * | 1997-12-01 | 1999-08-25 | 侯传绪 | Ozone water generator |
| CN2347966Y (en) * | 1998-06-18 | 1999-11-10 | 史腊求 | Energy-saving sewage aerator |
| EP1329254A1 (en) * | 2001-11-23 | 2003-07-23 | Hermann Böck | Device and process for mixing of liquid, viscous and/or pourable media |
| CN2636965Y (en) * | 2003-08-21 | 2004-09-01 | 福州上润精密仪器有限公司 | Gas and liquid mixed reactor |
| CN101219772A (en) * | 2006-09-21 | 2008-07-16 | 波克股份有限公司 | Gas mixing device and its application method |
| CN101042056A (en) * | 2007-04-30 | 2007-09-26 | 西安交通大学 | Grooving gaseous film cooling hole |
| CN101832154A (en) * | 2009-03-11 | 2010-09-15 | 中国科学院工程热物理研究所 | Method for cooling air film of turbine blade of aircraft engine |
| CN102166487A (en) * | 2011-03-13 | 2011-08-31 | 深圳乐满商务服务有限公司 | Vortex gas and liquid mixer |
| CN202017516U (en) * | 2011-03-21 | 2011-10-26 | 西安西科煤矿安全通风防灭火研究所有限公司 | Fireproof extinguishing foam generator for mining |
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| CN206103742U (en) * | 2016-09-29 | 2017-04-19 | 浙江览锐智能科技有限公司 | Energy storage formula tectorial membrane mixing arrangement of ozone water |
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| CN106334490A (en) | 2017-01-18 |
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