CN114832663A - Micro-nano bubble liquid generation system and water heater - Google Patents
Micro-nano bubble liquid generation system and water heater Download PDFInfo
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- CN114832663A CN114832663A CN202111673912.1A CN202111673912A CN114832663A CN 114832663 A CN114832663 A CN 114832663A CN 202111673912 A CN202111673912 A CN 202111673912A CN 114832663 A CN114832663 A CN 114832663A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 742
- 239000002101 nanobubble Substances 0.000 title claims abstract description 256
- 238000002156 mixing Methods 0.000 claims abstract description 281
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/0005—Details for water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H9/00—Details
- F24H9/20—Arrangement or mounting of control or safety devices
- F24H9/2007—Arrangement or mounting of control or safety devices for water heaters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Engineering & Computer Science (AREA)
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- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Accessories For Mixers (AREA)
- Multiple-Way Valves (AREA)
Abstract
The invention discloses a micro-nano bubble liquid generating system and a water heater, wherein the micro-nano bubble liquid generating system comprises an air dissolving device and an air inlet assembly. A mixing cavity is formed in the air dissolving device, and a liquid inlet flow path and an air inlet path which are communicated with the mixing cavity are formed on the air dissolving device. The air inlet assembly is connected with the air dissolving device, the air inlet assembly enables the air inlet path to inlet air towards the mixing cavity, and gas and liquid in the air dissolving device are mixed to form gas-liquid mixed liquid. The air inlet assembly further comprises a one-way valve, and the one-way valve is arranged on the air inlet path to control the air inlet direction of the air inlet path. The micro-nano bubble liquid generation system provided by the embodiment of the invention can realize efficient air intake and air dissolution and output a gas-liquid mixed solution, and the air dissolution does not need to cut off water.
Description
Cross Reference to Related Applications
The present application is based on the chinese patent application having application number 202120289186.2, application date 2021, No. 02/01, and claims priority from the chinese patent application, the entire contents of which are incorporated herein by reference.
Technical Field
The invention belongs to the technical field of household appliances, and particularly relates to a micro-nano bubble liquid generation system and a water heater.
Background
The micro-nano bubble water is formed by dissolving a large amount of micro bubbles with the bubble diameter of 0.1-50 mu m in water. The micro-nano bubble water is widely applied to industrial water treatment and water pollution treatment at present, and is gradually applied to daily life and beauty products at present.
The micro-nano bubbles have smaller size, so that the micro-nano bubbles can show the characteristics different from common bubbles, such as long existence time, higher interface zeta potential, high mass transfer efficiency and the like. By utilizing the characteristics of the micro-nano bubbles, the micro-nano bubble water can be prepared for degrading pesticide residues of vegetables and fruits, can kill bacteria and partial viruses, and has partial effect on antibiotics and hormones of some meats.
At present, micro-nano bubble water generation technology can be divided into the following steps according to a bubble generation mechanism: pressurized gas dissolving method, air entraining induction method and electrolytic precipitation method. Although bubbles formed by traditional pressurized dissolved air are fine, a booster pump is needed for pressurization, so that the system has large running amount, large running noise and vibration, high cost and low cost performance, and is not beneficial to being applied to small equipment; the series operation and control are complex, and the experience effect is poor.
In the production process of some micro-nano bubble water, in the process of dissolving gas in liquid to form gas-dissolved water, water cannot be discharged from a water using terminal, so that a user needs to wait for a period of time to use the micro-nano bubble water; even when micro-nano bubble water is used, the micro-nano bubble water cannot be continuously output when the micro-nano bubble water is not enough, and user experience is influenced.
Disclosure of Invention
The present invention is directed to solving at least one of the problems of the prior art. Therefore, the invention provides a micro-nano bubble liquid generation system which is stable and controllable in pressure, high in dissolved gas liquid generation efficiency and simple in system operation, and solves the technical problems of large amount, high cost and low cost performance of a traditional pressurizing dissolved gas operation in the prior art.
The invention also aims to provide a water heater with the micro-nano bubble liquid generation system.
According to the embodiment of the invention, the micro-nano bubble liquid generation system comprises: the air dissolving device is internally provided with a mixing cavity and is provided with a liquid inlet flow path and an air inlet path which are communicated with the mixing cavity; the gas inlet assembly is connected with the gas dissolving device, the gas inlet assembly enables the gas inlet gas path to inlet gas towards the mixing cavity, and gas and liquid in the gas dissolving device are mixed to form gas-liquid mixed liquid; the check valve is arranged on the air inlet path to control the air inlet direction of the air inlet path.
According to the micro-nano bubble liquid generation system provided by the embodiment of the invention, the air inlet assembly can rapidly inlet air towards the air dissolving device, so that the air dissolving device is filled with air; the gas dissolving device discharges liquid outwards in the gas inlet process, so that gas-liquid mixed liquid in the gas dissolving device can flow out to the water using end in the gas inlet process, water is not required to be cut off in the whole process, and guarantee is provided for the subsequent formation of micro-nano bubble water. In the process of air intake and liquid discharge, the one-way valve only allows the air in the air intake path to move towards the mixing cavity, so that the air intake and liquid discharge of the mixing cavity are reliable.
According to some embodiments of the present invention, the micro-nano bubble liquid generation system further includes a liquid path pressure regulating valve assembly, the liquid path pressure regulating valve assembly is disposed on the liquid inlet flow path, and the liquid path pressure regulating valve assembly is configured to regulate a pressure of the liquid inlet flow path.
According to the micro-nano bubble liquid generation system provided by some embodiments of the invention, the air inlet assembly comprises a pump body, the air dissolving device is provided with a liquid outlet flow path communicated with the mixing cavity, and the pump body is arranged on the liquid outlet flow path and used for pumping liquid in the air dissolving device, so that when the pressure of gas in the air dissolving device is smaller than that of gas in the air inlet flow path, the air inlet flow path introduces air into the mixing cavity.
Optionally, still be equipped with on the gas dissolving device with the flow path that converges that the hybrid chamber communicates, the one end of converging the flow path communicate respectively the feed liquor flow path with the gas circuit of admitting air, the other end intercommunication that converges the flow path the hybrid chamber, the pump body is established on converging the flow path.
According to the micro-nano bubble liquid generation system provided by some embodiments of the invention, the air intake assembly comprises an inflator pump, the inflator pump is arranged on the air intake path, and the inflator pump can inflate the mixing cavity.
According to a further embodiment of the invention, the micro-nano bubble liquid generating system further comprises a pressure stabilizing valve, and the pressure stabilizing valve is connected with the liquid path pressure regulating valve assembly in parallel.
Optionally, two ends of the pressure stabilizing valve are connected with the liquid path pressure regulating valve assembly in parallel and then are arranged on the liquid inlet path; or one end of a liquid separating flow path connected with the pressure stabilizing valve is connected to the liquid inlet end of the liquid path pressure regulating valve assembly, and the other end of the liquid separating flow path is connected to the liquid inlet end of the gas dissolving device; or one end of a liquid separating flow path connected with the pressure stabilizing valve is connected to the liquid inlet end of the liquid path pressure regulating valve component, and the other end of the liquid separating flow path is connected to the liquid outlet flow path of the mixing cavity.
Optionally, the liquid path pressure regulating valve assembly comprises a flow regulating valve, and the pressure stabilizing valve and the flow regulating valve are integrally arranged on the liquid inlet path.
Optionally, the liquid inlet flow path is communicated with the mixing cavity through a liquid inlet, and the air inlet path is communicated with the mixing cavity through an air inlet; the liquid path pressure regulating valve assembly comprises a water inlet valve and a pressure stabilizing valve, the liquid inlet flow path is provided with the water inlet valve for controlling the on-off of water flow in the liquid inlet flow path and the pressure stabilizing valve for stabilizing the water inlet pressure of the liquid inlet, and the air pressure pumped by the inflator pump is not less than the water inlet pressure of the liquid inlet; or the liquid path pressure regulating valve assembly comprises: and the pressure regulating valve is connected in series on the liquid inlet pipeline, and the water outlet pressure of the pressure regulating valve is adjustable between an upper threshold and a lower threshold.
Optionally, the water inlet valve and the pressure stabilizing valve are sequentially connected in series on the liquid inlet flow path; or the two ends of the water inlet valve are connected with the pressure stabilizing valve in parallel and then are connected with the liquid inlet flow path in series.
Optionally, the water inlet valve is a two-position three-way valve, the two-position three-way valve is provided with two water outlet water paths which are arranged in parallel, and the pressure stabilizing valve is connected in series with one of the two water outlet water paths.
Optionally, the pressure stabilizing valve is an adjustable pressure stabilizing valve, and the air pressure pumped by the inflator is not less than a lower threshold of an adjustable pressure range of the adjustable pressure stabilizing valve.
According to some embodiments of the present invention, the micro-nano bubble liquid generating system further includes: the controller is in communication connection with the inflator pump and is used for controlling the inflator pump to start and stop; or the controller is connected with the pump body of the air inlet assembly and used for controlling the pump body to start and stop.
According to a further embodiment of the present invention, the micro-nano bubble liquid generating system further includes: the water flow sensor is arranged on the liquid inlet flow path to detect the liquid inlet flow of the liquid inlet flow path; the water flow sensor is in communication connection with the controller; the controller is configured to control activation of the inflator or pump body when the water flow sensor detects a water flow signal.
Optionally, the controller still respectively with liquid way pressure regulating valve subassembly with the subassembly communication of admitting air is connected, the controller is used for when the accumulated discharge of rivers sensor is greater than first preset flow or the accumulated live time of rivers sensor is greater than first preset time, control liquid way pressure regulating valve subassembly switches to little water pressure state from big water pressure state, just the controller control the subassembly action of admitting air, in order to get into the state of admitting air.
Advantageously, the controller controls the pump body of the air intake assembly and/or controls the inflator of the air intake assembly to be activated when the liquid path pressure regulating valve assembly is switched to a low water pressure state.
According to some embodiments of the invention, the micro-nano bubble liquid generation system further comprises a micro-nano bubble generator and a water outlet piece, wherein the micro-nano bubble generator is connected with a liquid outlet flow path of the air dissolving device; the water outlet piece is connected to the tail end of the liquid outlet flow path, and the micro-nano bubble generator is arranged in the water outlet piece; the water outlet piece is a shower head or a faucet.
A water heater according to an embodiment of the present invention includes: a heating device; in the micro-nano bubble liquid generating system in each of the above examples, the air dissolving device of the micro-nano bubble liquid generating system is arranged at the water outlet end or the water inlet end of the heating device.
According to the water heater provided by the embodiment of the invention, by adopting the micro-nano bubble liquid generating system, the gas-dissolved liquid can be quickly formed in the water heater, and the gas-dissolved liquid with a certain temperature or the gas-dissolved liquid generated by the gas dissolving device is conveyed to the water outlet end of the water heater, so that a user can use water with required properties in time. The internal pressure of the water heater is adjusted stably, the operation is stable, the user experience is good, and the product safety is high.
Additional aspects and advantages of the invention will be set forth in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
Drawings
The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:
fig. 1 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the first aspect of the present invention, wherein a water flow sensor is disposed upstream of a pressure stabilizing valve.
Fig. 2 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the first aspect of the present invention, wherein a water flow sensor is disposed downstream of a pressure stabilizing valve.
Fig. 3 is a schematic control flow diagram of the micro-nano bubble liquid generation system shown in fig. 1.
Fig. 4 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the second aspect of the present invention, wherein a water flow sensor is disposed upstream of a pressure stabilizing valve.
Fig. 5 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the second aspect of the present invention, wherein a water flow sensor is disposed downstream of a pressure stabilizing valve.
Fig. 6 is a schematic control flow diagram of the micro-nano bubble liquid generation system shown in fig. 4.
Fig. 7 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the third aspect of the present invention, wherein a water flow sensor is disposed upstream of a pressure stabilizing valve.
Fig. 8 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the third aspect of the present invention, wherein a water flow sensor is disposed downstream of a pressure stabilizing valve.
Fig. 9 is a schematic control flow diagram of the micro-nano bubble liquid generating system shown in fig. 7.
FIG. 10 is a schematic view of a water heater according to some embodiments of the invention.
Fig. 11 is a schematic view of an air dissolving device.
Fig. 12 is a schematic diagram of a micro-nano bubble liquid generation system according to some embodiments of the fourth aspect of the present invention, wherein a water flow sensor is disposed upstream of a pressure regulating valve.
Fig. 13 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the fourth aspect of the present invention, wherein a water flow sensor is disposed downstream of a pressure regulating valve.
Fig. 14 is a control flow diagram of the micro-nano bubble liquid generating system shown in fig. 12.
FIG. 15 is a schematic view of a water heater according to other embodiments of the present invention in which the fluid line regulator valve assembly is a pressure regulator valve.
Fig. 16 is a schematic view of a micro-nano bubble liquid generating system according to some embodiments of the fifth aspect of the present invention, wherein a flow regulating valve and a pressure stabilizing valve are arranged in parallel, and a water flow sensor is arranged upstream of the pressure stabilizing valve and the flow regulating valve.
Fig. 17 is a schematic view of a micro-nano bubble liquid generating system according to some embodiments of the fifth aspect of the present invention, wherein a flow regulating valve and a pressure stabilizing valve are arranged in parallel, and a water flow sensor is arranged downstream of the pressure stabilizing valve and the flow regulating valve.
Fig. 18 is a schematic control flow diagram of the micro-nano bubble liquid generating system shown in fig. 16.
Fig. 19 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the sixth aspect of the present invention, wherein the air inlet assembly is a pump body and is disposed on the liquid outlet path, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 20 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the sixth aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the liquid outlet path, the flow regulating valve and the pressure stabilizing valve are disposed in parallel, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 21 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the sixth aspect of the present invention, in which the air inlet assembly is a pump body and is disposed on the liquid outlet path, the liquid outlet end of the liquid separating path of the pressure stabilizing valve is connected to the liquid outlet path, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 22 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the seventh aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the merging flow path, the flow regulating valve and the pressure stabilizing valve are disposed in parallel, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 23 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the seventh aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the converging flow path, the liquid outlet end of the liquid separation flow path of the pressure stabilizing valve is connected to the converging flow path behind the pump body, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 24 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the seventh aspect of the present invention, in which the air inlet assembly is a pump body and is disposed on the converging flow path, the liquid outlet end of the liquid separating flow path of the pressure stabilizing valve is connected to the liquid outlet flow path, and the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly.
Fig. 25 is a schematic control flow diagram of the micro-nano bubble liquid generating system shown in fig. 19.
Fig. 26 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of the eighth aspect of the present invention, wherein the air intake assembly is a pump body and is disposed on the liquid outlet path, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 27 is a schematic view of a micro-nano bubble liquid generating system according to some embodiments of an eighth aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the liquid outlet path, the flow regulating valve and the pressure stabilizing valve are disposed in parallel, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 28 is a schematic view of a micro-nano bubble liquid generating system according to some embodiments of an eighth aspect of the present invention, where the air intake assembly is a pump body and is disposed on the liquid outlet path, the liquid outlet end of the liquid dividing path of the pressure stabilizing valve is connected to the liquid outlet path, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 29 is a schematic view of a micro-nano bubble liquid generating system according to some embodiments of a ninth aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the merging flow path, the flow regulating valve and the pressure stabilizing valve are disposed in parallel, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 30 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of a ninth aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the merged flow path, the liquid outlet end of the liquid separation flow path of the pressure stabilizing valve is connected to the merged flow path behind the pump body, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 31 is a schematic diagram of a micro-nano bubble liquid generating system according to some embodiments of a ninth aspect of the present invention, in which the air intake assembly is a pump body and is disposed on the merging flow path, the liquid outlet end of the liquid separation flow path of the pressure stabilizing valve is connected to the liquid outlet flow path, the water flow sensor is disposed upstream of the liquid path pressure regulating valve assembly, and the liquid level sensor is disposed on the air dissolving device.
Fig. 32 is a schematic control flow diagram of the micro-nano bubble liquid generating system shown in fig. 26, wherein a liquid level sensor is arranged at the lower part of the mixing chamber.
FIG. 33 is a cross-sectional view of a flow control valve according to some embodiments of the present invention in a high water pressure state.
FIG. 34 is a cross-sectional view of a flow control valve according to some embodiments of the invention in a low water pressure state.
FIG. 35 is a cross-sectional view of an integrally-disposed, fluid line pressure regulator valve assembly according to some embodiments of the present invention.
Fig. 36 is a sectional view of the flow rate regulating valve of fig. 35 in a low water pressure state.
Fig. 37 is a sectional view of the flow rate adjustment valve of fig. 35 in a high water pressure state.
Fig. 38 is a cross-sectional view of the regulator valve of fig. 35 open.
Fig. 39 is a cross-sectional view of the regulator valve of fig. 35 closed.
FIG. 40 is a schematic view of a water heater according to further embodiments of the present invention, wherein the intake assembly is a pump and the pump is disposed in the outlet flow path.
FIG. 41 is a schematic flow diagram of a water heater according to some embodiments of the present invention, wherein the intake assembly is a pump body, and the pump body is disposed on a converging flow path, and the heating device is disposed between the pump body and the air dissolving device.
FIG. 42 is a schematic flow diagram of a water heater according to further embodiments of the present invention, wherein the intake assembly is a pump body disposed in the combined flow path and the heating device is disposed in the outlet flow path after the dissolving device.
Reference numerals:
100. a micro-nano bubble liquid generation system;
1. a gas dissolving device; 11. an air inlet; 12. a liquid inlet; 13. a liquid outlet;
14. a housing; 141. a first end cap; 142. a second end cap;
15. a partition plate; 151. a through hole; 16. a mixing chamber; 161. a liquid level sensor;
2. a power supply device; 3. a controller;
4. a water outlet member; 41. a micro-nano bubble generator;
5. an air inlet path; 50. an air intake assembly; 51. a one-way valve; 52. an inflator pump; 53. a pump body;
6. a liquid outlet flow path; 61. a water outlet switch;
7. a liquid inlet flow path; 70. a liquid path pressure regulating valve assembly; 71. a water flow sensor;
72. a pressure maintaining valve; 721. a pressure stabilizing housing; 722. a pressure stabilizing inlet; 723. a pressure stabilizing outlet; 724. an adjustment assembly;
73. a water pump;
74. a water inlet valve; 75. a two-position three-way valve; 76. an adjustable pressure maintaining valve; 77. a pressure regulating valve;
78. a flow regulating valve;
781. a valve housing; 7811. a valve inlet; 7812. a valve outlet;
782. a flow stabilizing assembly; 7821. a flow stabilizing valve core; 7822. a flow-stabilizing valve body;
783. a drive assembly; 7831. a drive member; 7832. a barrier;
791. a first tee joint; 792. a second tee joint;
8. a merged channel; 81. a liquid separation flow path; 82. a merging port;
1000. a water heater;
200. a cold water inlet flow channel; 300. a hot water outlet flow passage; 400. a heating device.
Detailed Description
Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the accompanying drawings are illustrative only for the purpose of explaining the present invention, and are not to be construed as limiting the present invention.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "back", "top", "bottom", "inner", "outer", "axial", and the like are used in the orientations and positional relationships indicated in the drawings, which are based on the orientation or positional relationship shown in the drawings, and are used for convenience in describing the present invention and for simplicity in description, and do not indicate or imply that the device or element so referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, are not to be construed as limiting the present invention.
The micro-nano bubble liquid generation system 100 according to the embodiment of the present invention is described below with reference to the drawings.
A micro-nano bubble liquid generating system 100 according to an embodiment of the present invention, as shown in the first aspect example in fig. 1 to 2, the second aspect example in fig. 4 to 5, the third aspect example in fig. 7 to 8, the fourth aspect example in fig. 12 to 13, the fifth aspect example in fig. 16 to 17, the example of the sixth aspect in fig. 19, 20, and 21, the example of the seventh aspect in fig. 22, 23, and 24, the example of the eighth aspect in fig. 26, 27, and 28, and the ninth aspect example in fig. 29 to 31, includes: the air dissolving device 1, the liquid path pressure regulating valve assembly 70 and the air inlet assembly 50.
Wherein, a mixing cavity 16 is formed in the air dissolving device 1, and a liquid inlet flow path 7 and an air inlet path 5 which are communicated with the mixing cavity 16 are formed on the air dissolving device 1. The inlet flow path 7 may introduce liquid into the mixing chamber 16 and the inlet gas path 5 may introduce gas into the mixing chamber 16.
Further, the air inlet assembly 50 is connected with the air dissolving device 1, the air inlet assembly 50 enables the air inlet path 5 to inlet air to the mixing cavity 16, and at the moment, the air in the mixing cavity 16 is increased continuously; and the gas and the liquid in the gas dissolving device 1 are mixed to form a gas-liquid mixed liquid.
The air intake assembly 50 includes a check valve 51, and the check valve 51 is provided on the air intake path 5 to control an air intake direction of the air intake path 5.
According to the structure, in the micro-nano bubble liquid generation system 100 provided by the embodiment of the invention, the air inlet assembly 50 can quickly inlet air towards the air dissolving device 1, so that the air dissolving device 1 is filled with air; dissolve gas device 1 outwards discharges liquid simultaneously at the process of admitting air to the gas-liquid mixture in the in-process that admits air dissolves gas device 1 can flow out to the water end, and whole process need not to cut off water, provides the guarantee for follow-up formation micro-nano bubble water. The one-way valve 51 is provided to allow the gas in the gas inlet path 5 to move toward the mixing chamber 16 during the gas inlet and liquid outlet processes, so that the gas inlet and liquid outlet operations of the mixing chamber 16 are reliable.
Compared with the pressurizing and air dissolving method which needs a booster pump for pressurization in the prior art, the invention has the advantages of simple structure and low cost; the whole body is modularized, the size is small, the arrangement is compact, the device is convenient to be used on small equipment, and the occupied size can be changed to meet different use scenes; the cost performance of the product is improved, the air inlet and air dissolving process is simple to control, water can not be cut off at the water end, the air can be filled midway, the condition of water flow closing does not exist, the user experience is good, and the starting speed of the whole machine is improved.
It should be noted that the liquid in the present invention refers to a liquid in which a certain gas is dissolved, or a heated liquid, or a tap water with a certain impurity and a lower temperature, or a purified water purified by a purification device, or a relatively pure water supplied to a living water tank, and the water inlet described in the present invention refers to a liquid inlet mainly, and the water outlet refers to a liquid outlet mainly, which should be understood widely, and should not be limited to the water described in the chemical field.
In some embodiments of the present invention, the liquid passage pressure regulating valve assembly 70 in the above example is provided on the intake liquid flow passage 7, the liquid passage pressure regulating valve assembly 70 is used to regulate the pressure of the intake liquid flow passage 7, and the liquid passage pressure regulating valve assembly 70 has a large water pressure state and a small water pressure state, that is, the liquid passage pressure regulating valve assembly 70 can regulate the gas pressure and the water pressure in the gas dissolving apparatus 1, thereby changing the internal state of the mixing chamber 16.
Correspondingly, when the liquid path pressure regulating valve assembly 70 is in a low water pressure state, the air dissolving device 1 is in an air inlet state and the air inlet assembly 50 is operated, so that the air inlet path 5 is enabled to inlet air to the mixing cavity 16; when the liquid path pressure regulating valve assembly 70 is in a high water pressure state, the gas dissolving device 1 is in a gas dissolving state and the gas in the mixing chamber 16 is dissolved with the liquid phase to form a gas dissolving liquid.
The air inlet assembly 50 cooperates with the liquid path pressure regulating valve assembly 70 to regulate the pressure of the liquid inlet flow path 7, so as to keep the pressure of the liquid inlet end of the air dissolving device 1 at a preset value, and change the flow rate of the liquid in the liquid inlet flow path 7 and the air pressure in the mixing cavity 16.
Then, when the liquid path pressure regulating valve assembly 70 is switched to a low water pressure state, a small amount of liquid is formed in the liquid inlet flow path 7 at this time, the amount of liquid flowing out of the mixing cavity 16 is larger than the amount of liquid flowing in, the air pressure in the mixing cavity 16 is reduced, and after the air pressure in the mixing cavity 16 is smaller than the air pressure in the air inlet path 5, the gas in the gas source communicated with the air inlet path 5 can be charged into the mixing cavity 16, so that the gas can be rapidly charged toward the gas dissolving device 1 on the premise that the water pressure of the liquid inlet flow path 7 is stable, so that the required gas is charged into the gas dissolving device 1, and the gas charging process of the gas dissolving device 1 is realized. Meanwhile, as a certain amount of liquid is always stored in the air dissolving device 1 and the air dissolving device 1 keeps feeding liquid, the liquid can be discharged from the liquid outlet flow path 6 to the water using end all the time in the air feeding process of the air dissolving device 1, and the water cut is prevented.
After the gas dissolving device 1 is filled with more gas, the liquid path pressure regulating valve assembly 70 is switched to a high water pressure state, at the moment, the liquid inlet flow path 7 forms large flow liquid inlet, the amount of the liquid flowing into the mixing cavity 16 is larger than the amount of the liquid flowing out, so that more liquid flows into the mixing cavity 16 rapidly to stably increase the pressure in the mixing cavity 16, the gas filled into the gas dissolving device 1 is further promoted to be dissolved into the liquid rapidly to form gas dissolving liquid, and reliable guarantee is provided for the subsequent further generation of micro-nano bubble water.
It can be seen that, in the present invention, the air inlet assembly 50 and the liquid path pressure regulating valve assembly 70 are matched with each other, so that the air dissolving device 1 can be greatly facilitated to perform air inlet and air dissolving, and water can be always supplied to a user.
In some embodiments of the present invention, as shown in the sixth aspect example of fig. 19, 20, 21, the seventh aspect example of fig. 22, 23, and 24, the eighth aspect example of fig. 26, 27, and 28, and the ninth aspect example of fig. 29-31, the intake assembly 50 includes a pump body 53, and the pump body 53 draws liquid to cause the intake air path 5 to intake air toward the mixing chamber 16 in a low water pressure state. In these examples, since the liquid amount flowing into the mixing chamber 16 from the liquid inlet flow path 7 is small under a small water pressure, the pump body 53 can rapidly pump out the liquid at the corresponding position, so as to form a low-pressure region with a pressure lower than the pressure of the air source outside the air inlet path 5, so as to promote the air source to enter the low-pressure region, and finally, the air dissolving device 1 is filled with more air.
It should be noted that the pump body 53 may be a common water pump for pumping water.
For example, as shown in fig. 19, 20, and 21, which are examples of a sixth aspect, and fig. 26, 27, and 28, which are examples of an eighth aspect, the gas dissolving device 1 is formed with a liquid outlet flow path 6 communicating with the mixing chamber 16, and the pump body 53 is provided on the liquid outlet flow path 6 for pumping the liquid in the gas dissolving device 1 so that the gas pressure in the gas dissolving device 1 is lower than the gas pressure in the gas inlet path 5, and the gas inlet path 5 introduces gas into the mixing chamber 16. In these examples, when the pressure regulating valve assembly 70 is in a low pressure state, the liquid flow rate entering the liquid inlet flow path 7 to the mixing chamber 16 is small, and during the pumping process of the pump body 53, the liquid in the mixing chamber 16 will decrease sharply, so that the air pressure in the mixing chamber 16 with a certain volume is reduced, and a certain low pressure area is formed in the mixing chamber 16; meanwhile, the air pressure in the mixing chamber 16 is also rapidly reduced to be lower than the air pressure of the air source supply system connected with the air inlet path 5, at this time, the air can rapidly inflate into the mixing chamber 16 through the air inlet path 5, so that the mixing chamber 16 completes efficient air inlet, and the pressure in the mixing chamber 16 is relatively stable.
On the contrary, when the pump body 53 stops pumping, the liquid path pressure regulating valve assembly 70 is in a state of high water pressure and rapidly discharges liquid toward the mixing chamber 16, so that the gas space in the liquid inlet flow path 7 is sharply reduced, the pressure in the gas dissolving device 1 is increased, and the gas previously entering the mixing chamber 16 can be more rapidly dissolved into the liquid to form gas-dissolved liquid.
For another example, as shown in the seventh example of fig. 22, 23, and 24 and the ninth example of fig. 29 to 31, the air dissolving device 1 is further provided with a merging channel 8 communicating with the mixing chamber 16, one end of the merging channel 8 communicates with the intake channel 7 and the intake air channel 5, respectively, and the other end of the merging channel 8 communicates with the mixing chamber 16. Both the gas and the liquid can now enter the mixing chamber 16 through the converging flow path 8.
Further, the pump body 53 is provided on the merging flow path 8, and in a low water pressure state, the pump body 53 pumps the liquid to make the intake air path 5 intake the mixing chamber 16, and specifically, the pump body 53 pumps the liquid at the rear of the liquid path pressure regulating valve assembly 70, so that the liquids in the intake flow path 7 to the mixing chamber 16 are rapidly reduced and form a certain low pressure region, and the liquid pumped by the pump body 53 is discharged into the mixing chamber 16, and the low pressure region is simultaneously connected with the intake air path 5, so that the low pressure region will rapidly make the gas in the gas source supply system connected with the intake air path 5 enter the mixing chamber 16 through the merging flow path 8, thereby filling the mixing chamber 16 with the required gas amount.
On the contrary, the liquid amount of the liquid inlet flow path 7 is large under the large water pressure state, so that the liquid quickly enters the mixing chamber 16 through the converging flow path 8, the pump body 53 stops running, the space rich in air in the mixing chamber 16 is quickly filled with the liquid, the pressure of the gas dissolving device 1 is further increased, and the gas dissolving device 1 enters the gas dissolving state, so that the gas entering the mixing chamber 16 can be dissolved in the liquid and form a sufficient amount of gas dissolving liquid for subsequent use.
In some embodiments of the present invention, as shown in the first aspect example in fig. 1-2, the second aspect example in fig. 4-5, the third aspect example in fig. 7-8, the fourth aspect example in fig. 12-13, and the fifth aspect example in fig. 16-17, the intake assembly 50 includes an inflator 52, the inflator 52 is disposed on the intake air path 5, and the inflator 52 may inflate the mixing chamber 16. The inflator 52 is used for pumping air into the air dissolving device 1, and the air pressure pumped by the inflator 52 is greater than or equal to the pressure in the air dissolving device 1, so that the inflator 52 actively pumps the air into the mixing cavity 16, the air intake of the mixing cavity 16 is realized, and the air intake efficiency of the mixing cavity 16 is improved.
In some examples, the inflator 52 alone may be used to achieve air intake control and efficient air intake of the mixing chamber 16, such as the first aspect example in fig. 1-2, the second aspect example in fig. 4-5, the third aspect example in fig. 7-8, the fourth aspect example in fig. 12-13, and the fifth aspect example in fig. 16-17.
In other examples, the inflator 52 may also be used in the foregoing examples with the pump body 53, such as in the examples of the sixth aspect in fig. 19, 20, 21, the examples of the seventh aspect in fig. 22, 23, and 24, the examples of the eighth aspect in fig. 26, 27, and 28, and the examples of the ninth aspect in fig. 29-31, so as to implement the combination of the inflator 52 and the pump body 53.
In a specific example, the pump body 53 can pump liquid to reduce the pressure in the mixing chamber 16 or reduce the pressure in the liquid inlet flow path 7, and then the inflator 52 is actively operated to raise the pressure in the air inlet path 5, so that the pressure difference between the air pressure pumped by the inflator 52 and the pressure in the air dissolving device 1 is larger, the air inlet of the mixing chamber 16 is controlled more quickly, and the efficient air inlet of the mixing chamber 16 is easier to realize. The above examples are intended to fall within the scope of the present invention.
Alternatively, in examples where the aforementioned aspects are provided with an inflator 52, the check valve 51 inflates the inflator 52 towards the mixing chamber 16. The one-way valve 51 can effectively control the flowing direction of the air flow in the air inlet path 5, so that the air flow can only be inflated from the inflator 52 to the mixing chamber 16 in one direction, but not in the opposite process, thereby ensuring that the pressure between the air inlet path 5 and the air dissolving device 1 is controllable, and preventing the air dissolving device 1 from releasing pressure or even being incapable of air inlet.
Of course, in various examples without the inflator 52, the check valve 51 may be disposed on the air intake path 5, so that the air of the air source connected to the air intake path 5 can flow into the air dissolving device 1 in one direction, and does not flow back to the air source from the air dissolving device 1 in the opposite direction, thereby ensuring that the pressure of the air dissolving device 1 after air intake is controllable.
As shown in the fifth aspect example in fig. 16-17, the sixth aspect example in fig. 20 and 21, the seventh aspect example in fig. 22, 23 and 24, the eighth aspect example in fig. 27 and 28, and the ninth aspect example in fig. 29-31, the micro-nano bubble liquid generating system 100 further includes a pressure stabilizing valve 72, the pressure stabilizing valve 72 is arranged in parallel with the liquid path pressure regulating valve assembly 70, and the pressure stabilizing valve 72 can ensure the pressure at the liquid inlet end of the air dissolving device 1, so that the air dissolving device 1 can be fed with liquid under a certain pressure; smooth air intake of the air intake path 5 can also be achieved by selecting the pressure maintaining valves 72 having different pressures. In a specific example, if the water outlet pressure of the pressure stabilizing valve 72 is P1, the air outlet pressure of the inflator 52 is P2, and the pressure P2 is controlled to be equal to or greater than P1, smooth liquid inlet of the liquid inlet flow path 7 can be realized, and smooth air inlet of the air inlet air path 5 is ensured.
Alternatively, as shown in each example of fig. 16, 17, 20, 22, 27 and 29, both ends of the regulator valve 72 may be provided in the intake passage 7 in parallel with the pressure regulating valve unit 70. In these examples, the pressure stabilizing valve 72 and the water inlet end of the liquid path pressure regulating valve assembly 70 intersect and are connected with a water source through a pipeline, and the pressure stabilizing valve 72 and the water outlet end of the liquid path pressure regulating valve assembly 70 intersect and then converge into the air dissolving device 1, so that after the water pressure is regulated by the pressure stabilizing valve 72, the pressure and the water flow of one end of the liquid inlet connected with the air dissolving device 1 are regulated and controlled, and a certain amount of liquid is ensured to be contained in the air dissolving device 1, and the water using end is not cut off.
In these examples, the liquid path pressure regulating valve assembly 70 may select its own flow regulating valve 78 capable of regulating the flow, and when the pressure stabilizing valve 72 operates, the liquid outlet flow of the liquid inlet flow path 7 is the sum of the liquid outlet flow of the flow regulating valve 78 and the liquid outlet flow of the pressure stabilizing valve 72; when the pressure stabilizing valve 72 is closed, the liquid outlet flow of the liquid inlet flow path 7 is the liquid outlet flow of the flow regulating valve 78. The liquid path pressure regulating valve assembly 70 can also select a normally open valve which can be opened and closed, and when the pressure stabilizing valve 72 operates and the normally open valve is closed, the liquid outlet flow of the liquid inlet flow path 7 is the liquid outlet flow of the pressure stabilizing valve 72; when the pressure stabilizing valve 72 is closed and the normally open valve is opened, the liquid outlet flow of the liquid inlet flow path 7 is the liquid outlet flow of the normally open valve, so that different liquid outlet flow regulation under different liquid inlet pressures is realized.
Alternatively, in the examples shown in fig. 23 and 30, one end of the liquid separation flow path 81 connected to the pressure stabilizing valve 72 is connected to the liquid inlet end of the liquid path pressure regulating valve assembly 70, and the other end is connected to the liquid inlet end of the air dissolving device 1, in these examples, the hydraulic pressure of the liquid inlet flow path 7 can be adjusted, so that the liquid outlet flow rate in the liquid inlet flow path 7 can be adjusted, and a certain amount of water can be kept in the air dissolving device 1 without water cut-off. The liquid passage pressure regulating valve assembly 70 in these examples may be a flow regulating valve 78 or a normally open valve that can regulate the flow rate thereof, and the liquid separation flow passage 81 may be connected to the rear end of the pump body 53 in order to reduce the pumping pressure of the pump body 53, so that the pump body 53 only pumps the liquid in the liquid inlet flow passage 7 and does not need to pump the liquid in the liquid separation flow passage 81. For the liquid flow rate finally entering the air dissolving device 1, see the determination manner of the liquid outlet flow rate of the liquid inlet flow path 7 in the example in which the two ends of the pressure stabilizing valve 72 are connected in parallel with the liquid path pressure regulating valve assembly 70 and then are arranged on the liquid inlet flow path 7 in the previous example.
Or, in the examples shown in fig. 21, 24, 28 and 31, one end of the liquid separation flow path 81 connected to the pressure stabilizing valve 72 is connected to the liquid inlet end of the liquid path pressure regulating valve assembly 70, and the other end is connected to the liquid outlet flow path 6 of the mixing chamber 16, in these examples, after the pressure stabilizing valve 72 is opened, part of the liquid can also enter the liquid outlet flow path 6 through the liquid separation flow path 81, the pressure stabilizing valve 72 can further mix the dissolved gas liquid in the mixing chamber 16 with the water in the liquid separation flow path 81 while adjusting the water pressure in the liquid inlet flow path 7, so as to flow out toward the micro-nano water end together, so that the pressure of the whole bubble liquid generating system 100 is stabilized, and the liquid outlet flow path 6 can keep a certain amount of water outlet, thereby preventing the system from water cut-off. The liquid path pressure regulating valve assembly 70 in these examples can select the flow regulating valve 78 or the normally open valve which can regulate the flow, at this time, the liquid outlet flow of the pressure stabilizing valve 72 does not influence the liquid inlet flow of the air dissolving device 1, the liquid inlet flow of the air dissolving device 1 is equal to the liquid outlet flow of the flow regulating valve 78 or equal to the liquid outlet flow of the normally open valve, and the liquid separating flow path 81 is connected to the liquid outlet flow path 6, so when the pressure stabilizing valve 72 is opened, part of the liquid passing through the pressure stabilizing valve 72 can further flow into the water using end, and the water cut-off is prevented. The surge tank valve 72 in these examples is mainly a surge tank valve 72 that is generally used to realize open/close pressure regulation.
Therefore, in the present invention, when the pressure maintaining valve 72 is provided, the position of the pressure maintaining valve 72 can be appropriately adjusted according to actual needs.
Advantageously, a liquid inlet one-way valve can be arranged on the liquid separation flow path 81, so that the liquid flows from the pressure stabilizing valve 72 to the liquid outlet end without the opposite direction, and the pressure stability of the system is ensured.
Optionally, the pressure regulating valve assembly 70 for the liquid path adopts a flow regulating valve 78, the flow regulating valve 78 may be a flow valve with a continuously adjustable opening, the structure of the flow valve with a continuously adjustable opening may change the flow in the path by the rotation of a valve plate, and the specific rotation implementation form of the valve plate is not described herein; the flow switching valve can also realize variable output of multi-gear liquid outlet flow.
The flow switching valve with variable output of multi-gear output liquid flow is mainly described as outputting two-gear output liquid flow.
As shown in fig. 33 and 34, the flow switching valve includes a valve housing 781 having a valve inlet 7811 and a valve outlet 7812 that are communicable, a flow stabilizing assembly 782, and a driving assembly 783. The flow stabilizing assembly 782 and the driving assembly 783 are arranged in the valve casing 781 and divide the valve casing 781 into a first cavity and a second cavity, the first cavity is communicated with the valve inlet 7811, the second cavity is communicated with the valve outlet 7812, a first water passing channel communicated with the first cavity and the second cavity is formed in the middle of the flow stabilizing assembly 782, and a second water passing channel communicated with the first cavity and the second cavity is formed at one end of the flow stabilizing assembly 782; the driving assembly 783 can control the on-off of the first water passing channel or the second water passing channel, so that the water yield of the valve outlet 7812 can be adjusted.
Alternatively, as shown in fig. 33 and 34, the flow stabilization assembly 782 includes a flow stabilization valve spool 7821 and a flow stabilization valve body 7822, the flow stabilization valve body 7822 being disposed within the valve housing 781, the flow stabilization valve body 7822 having opposite ends directed toward the valve inlet 7811 and valve outlet 7812, respectively; the flow stabilizing valve core 7821 is arranged in the flow stabilizing valve body 7822, and a first water passing channel is formed in the flow stabilizing valve core 7821; a second water passing channel is formed at the edge of the steady flow valve body 7821 close to the driving assembly 783, and when the output end of the driving assembly 783 moves towards the position close to the second water passing channel, the second water passing channel is closed, so that the liquid entering from the valve inlet 7811 can only flow out from the first water passing channel to the valve outlet 7812, and at the moment, the flow switching valve is in a low water pressure state and outputs a low flow, which is beneficial to the air dissolving device 1 to realize air inlet; when the output end of the driving component 783 moves towards the direction far away from the second water passing channel, the second water passing channel is opened, so that liquid entering from the valve inlet 7811 can flow out from the first water passing channel to the valve outlet 7812, and liquid entering from the valve inlet 7811 can flow out from the second water passing channel to the valve outlet 7812, at the moment, the flow switching valve is in a large water pressure state, and the output of the flow switching valve is large in flow, and the gas dissolving device 1 is facilitated to realize gas dissolving.
Alternatively, as shown in fig. 33 and 34, the driving assembly 783 comprises a driving member 7831 and a blocking member 7832, the blocking member 7832 is connected to the output end of the driving member 7831, and the blocking member 7832 can move relative to the second water passage to open or close the second water passage. The outer contour of the barrier 7832 is preferably configured and dimensioned to completely block the second water passage, such that the second water passage is completely blocked when the barrier 7832 is closed over the second water passage.
Alternatively, the driving member 7831 can be selected from a cylinder, a stepping motor or an electric push rod, as long as the stepping movement of the blocking member 7832 can be achieved, and is not particularly limited herein.
Alternatively, the blocking member 7832 may be made of a partition, a diaphragm, a sealing plug, etc., as long as it can block the second water passage, and is not limited herein.
It is to be noted that the flow rate adjustment valve 78 in the present invention may also be used in the example shown in fig. 19, fig. 26, in which the pressure maintaining valve 72 is not provided, and is not limited to the example that occurs simultaneously with the pressure maintaining valve 72. In each example in which only the flow rate adjustment valve 78 is provided, the inlet flow rate in the air dissolving device 1 depends on the magnitude of the outlet flow rate of the flow rate adjustment valve 78.
The following describes in detail an integrated adjustable flow valve with integrated pressure maintenance valve 72 and flow control valve 78.
As shown in fig. 35, when the pressure-maintaining valve 72 and the flow-regulating valve 78 are integrally provided on the inlet flow path 7, the integrated variable flow valve has a valve inlet end and a valve outlet end, and the liquid entering from the valve inlet end can flow to the valve outlet end through the pressure-maintaining valve 72 being opened, or the liquid entering from the valve inlet end can flow to the valve outlet end through the flow-regulating valve 78. Because the flow regulating valve 78 can always maintain a certain flow capacity, the valve outlet end of the integrated adjustable flow valve always has a certain outlet flow.
The flow rate control valve 78 is selected from the flow rate switching valves described above, and the flow rate of the flow rate switching valve in a low water pressure state is assumed to be L Small The flow rate of the flow rate switching valve in a high water pressure state is L Big (a) The outlet pressure of the flow switching valve is P Valve with a valve body The liquid outlet flow of the flow switching valve is L Valve with a valve body (ii) a Pressure regulator valve 72 has a pressure P Voltage stabilization The liquid outlet flow of the pressure stabilizing valve 72 is L Voltage stabilization (ii) a The liquid outlet pressure of the integrated adjustable flow valve is P Go out The liquid outlet flow of the integrated adjustable flow valve is L Go out 。
When the integrated adjustable flow valve is in a steady flow and steady pressure state or a low flow state, the driving component 783 closes the second water passing channel of the flow switching valve, so that liquid can only flow out through the first water passing channel but not from the second water passing channel, and L can be obtained at the moment Valve with a valve body ＝L Small (ii) a When P is designed Voltage stabilization ≥P Valve with a valve body Then the surge valve 72 opens and final P Go out ＝P Voltage stabilization ，L Go out ＝L Small +L Voltage stabilization (ii) a When P is designed Voltage stabilization <P Valve with a valve body Then surge valve 72 is closed and final P Go out ＝P Valve with a valve body ，L Go out ＝L Small 。
When the integrated adjustable flow valve is in a large-flow state, the driving component 783 opens the second water passing channel of the flow switching valve, so that liquid can flow out through the first water passing channel and the second water passing channel, and L can be obtained at the moment Valve with a valve body ＝L Small +L Big (a) (ii) a When P is designed Voltage stabilization ≥P Valve with a valve body Then the surge valve 72 opens and final P Go out ＝P Voltage stabilization ，L Go out ＝L Small +L Big (a) +L Voltage stabilization (ii) a When P is designed Voltage stabilization <P Valve with a valve body Then surge valve 72 is closed and final P Go out ＝P Valve with a valve body ，L Go out ＝L Small +L Big (a) 。
Therefore, the pressure stabilizing valve 72 not only can stabilize the liquid outlet pressure of the integrated adjustable flow valve when being opened, but also can adjust the liquid outlet flow of the integrated adjustable flow valve. When the pressure stabilizing valve 72 is closed, the liquid outlet pressure of the integrated adjustable flow valve is adjusted through the liquid outlet pressure of the flow switching valve, and the liquid outlet flow of the integrated adjustable flow valve can form different large-flow water outlets, so that the liquid inlet in the gas dissolving device 1 can be always kept and the gas dissolving device cannot be completely closed.
It should be noted that the integrated adjustable flow valve of the present invention is mainly applied to the case where both ends of a regulator valve 72 shown in each example of fig. 16, 17, 20, 22, 27, and 29 are connected in parallel with a liquid path pressure regulating valve assembly 70 and then provided on the liquid inlet flow path 7.
When the integrated adjustable flow valve is not used, two pipelines can be used for enabling the pressure stabilizing valve 72 and the flow regulating valve 78 to be connected in parallel and arranged in a split mode.
Further, as shown in fig. 35, the liquid path pressure regulating valve assembly 70 further includes a first tee 791 and a second tee 792, a water inlet end of the first tee 791 is communicated with the liquid inlet flow path 7, and two water outlet ends of the first tee 791 are respectively communicated with a water inlet side of the pressure maintaining valve 72 and a water inlet side of the flow regulating valve 78; two water inlet ends of the second tee 792 are respectively communicated with the water outlet side of the flow regulating valve 78 and the water outlet side of the pressure stabilizing valve 72, and the water outlet end of the second tee 792 is communicated with the gas dissolving device 1.
That is, the first tee 791 is connected to the pressure maintaining valve 72 and the flow regulating valve 78, and two flow paths in the first tee 791 are respectively communicated with the pressure maintaining valve 72 and the flow regulating valve 78, so that the liquid is respectively shunted to the pressure maintaining valve 72 or the flow regulating valve 78 through the first tee 791.
Similarly, the second tee 792 is also connected with the pressure stabilizing valve 72 and the flow regulating valve 78 respectively, and two flow paths of the second tee 792 are communicated with the pressure stabilizing valve 72 and the flow regulating valve 78 respectively, so that liquid in the pressure stabilizing valve 72 can flow out through the second tee 792, or liquid in the flow regulating valve 78 can flow out through the second tee 792, and finally the whole integrated adjustable flow valve is compact in structure, small and exquisite and convenient to install, the liquid outlet pressure regulating effect is good, the liquid outlet flow is adjustable, the air dissolving device 1 is convenient to realize quick air dissolving after air inlet, and water end water supply can be guaranteed.
In the description of the present invention, the features defined as "first" and "second" may explicitly or implicitly include one or more of the features for distinguishing between the described features, whether they are sequential or not.
In a specific example, the first three-way 791 is in threaded or snap connection with the water inlet side of the pressure maintaining valve 72 and the water inlet side of the flow regulating valve 78, so that the first three-way 791 is connected with the pressure maintaining valve 72.
In other examples, the integral connection of the first tee 791 and the pressure maintaining valve 72 may also be made by welding, and the integral connection of the first tee 791 and the flow regulating valve 78 may also be made by welding. Similarly, the second tee 792 is connected with the pressure maintaining valve 72 by screw or snap connection with the water outlet side of the pressure maintaining valve 72 and the water outlet side of the flow regulating valve 78. In other examples, the integral connection of the second tee 792 and the regulator valve 72 may also be achieved by welding, and the integral connection of the second tee 792 and the flow control valve 78 may also be achieved by welding.
Optionally, the two water outlet ends of the first tee 791 and the two water inlet ends of the second tee 792 correspond to and are coaxially disposed with each other, thereby reducing resistance to over-flow. In cooperation with the pressure stabilizing valve 72, the water inlet side and the water outlet side of the pressure stabilizing valve are coaxially arranged with the water outlet end of the corresponding first tee 791 and the water inlet end of the corresponding second tee 792, so that the pressure stabilizing valve is convenient to connect and has small water passing resistance; the water inlet side and the water outlet side of the flow regulating valve 78 are also coaxially arranged with the water outlet end of the corresponding first tee 791 and the water inlet end of the corresponding second tee 792, so that the connection is convenient and the water passing resistance is small.
As shown in FIGS. 36 and 37, in order to provide the flow control valve 78 in the integrated variable flow valve, the flow control valve 78 should be matched in size to the outlet end of the first tee 791 and the inlet end of the second tee 792, and corresponding screw or groove fittings are provided on the inner walls of the flow control valve 78 on the inlet side and the outlet side.
Alternatively, as shown in fig. 38 and 39, a schematic view of a surge damping valve 72 provided in an integrated adjustable flow valve is shown. The pressure stabilizing valve 72 comprises a pressure stabilizing shell 721 and an adjusting component 724 arranged in the pressure stabilizing shell 721, a pressure stabilizing inlet 722 and a pressure stabilizing outlet 723 which are communicated are arranged in the pressure stabilizing shell 721, a pressure stabilizing runner communicated with the pressure stabilizing inlet 722 and the pressure stabilizing outlet 723 is arranged in the pressure stabilizing shell 721, and the adjusting component 724 can conduct or cut off the pressure stabilizing runner when moving, so that the pressure stabilizing valve 72 is in an open state when the adjusting component 724 conducts the pressure stabilizing runner; when the regulating member 724 blocks the pressure-stabilizing flow passage, the pressure-stabilizing valve 72 is in a closed state.
Advantageously, the adjusting assembly 724 may include a solenoid rod assembly and an electromagnetic mating piece, which form a magnetic attraction when the solenoid rod assembly and the electromagnetic mating piece are energized to cut off the voltage stabilizing flow passage; when the electromagnetic valve component and the electromagnetic matching piece are powered off, the voltage stabilizing flow passage is conducted.
In order to keep the electromagnetic valve rod assembly at a specific position, an elastic reset piece is arranged between the electromagnetic valve rod assembly and the electromagnetic matching piece, so that after the electromagnetic valve rod assembly and the electromagnetic matching piece are powered off, the reset force of the elastic reset piece drives the electromagnetic valve rod assembly to move towards one side far away from the electromagnetic matching piece to open the pressure stabilizing flow channel.
Of course, the adjusting assembly 724 is not limited to the solenoid rod assembly and the electromagnetic mating member, and for example, in other examples, the adjusting assembly may be in the form of an electric push rod or an air cylinder driven sealing plug, which is not limited herein.
Alternatively, the telescopic movement direction of the adjusting assembly 724 is perpendicular to a connecting line formed by the pressure stabilizing inlet 722 and the pressure stabilizing outlet 723, so that the pressure stabilizing flow passage can be reliably intercepted when the adjusting assembly 724 changes posture.
Various examples of intake assembly 50 using only inflator 52 are described below.
As shown in the first aspect example in fig. 1 to 2, the second aspect example in fig. 4 to 5, the third aspect example in fig. 7 to 8, the fourth aspect example in fig. 12 to 13, and the fifth aspect example in fig. 16 to 17, the inlet flow path 7 communicates with the mixing chamber 16 through the inlet 12, the inlet gas path 5 communicates with the mixing chamber 16 through the inlet 11, the mixing chamber 16 is further provided with the outlet 13, and the outlet 13 communicates with the outlet flow path 6.
That is, the gas dissolving device 1 has a liquid inlet 12, a gas inlet 11 and a liquid outlet 13 through its container wall, wherein the mixing chamber 16 is communicated with an external flow path or gas path through the liquid inlet 12, the gas inlet 11 and the liquid outlet 13.
Further, as shown in the first aspect example in fig. 1-2 and the second aspect example in fig. 4-5, the liquid path pressure regulating valve assembly 70 includes a water inlet valve 74 and a pressure maintaining valve 72, the liquid inlet flow path 7 is provided with a water inlet valve 74 for controlling the on-off of the water flow in the liquid inlet flow path 7 and a pressure maintaining valve 72 for stabilizing the water inlet pressure of the liquid inlet 12, and the air pressure pumped by the inflator 52 is not less than the water inlet pressure of the liquid inlet 12. That is, in these examples, the pressure maintaining valve 72 is provided before the inlet 12 simultaneously with the inlet valve 74. The pressure stabilizing valve 72 is used for stabilizing water inlet pressure, and when the water pressure of tap water is unstable, the pressure stabilizing valve 72 can stabilize the water pressure of tap water to be not more than a preset water pressure value, so that the stability of the water pressure of the micro-nano bubble liquid generation system 100 is ensured, and the safety and the reliability of the micro-nano bubble liquid generation system 100 are improved.
When the micro-nano bubble liquid generating system 100 is used, water enters the mixing cavity 16 of the air dissolving device 1 through the liquid inlet 12, air becomes air with higher pressure after passing through the inflator pump 52, the air enters the mixing cavity 16 of the air dissolving device 1 through the air inlet 11 to enable the mixing cavity 16 to contain sufficient amount of gas, the water and the air are fully mixed in the mixing cavity 16 of the air dissolving device 1 to form solution liquid, and the solution flows out through the liquid outlet 13 and then passes through the micro-nano bubble generator 41 to become micro-nano bubble water for users to use.
According to the micro-nano bubble liquid generating system, the water inlet valve 74 and the pressure stabilizing valve 72 are arranged on the liquid inlet flow path 7, the stability of water inlet pressure is improved, the inflator pump 52 is arranged on the air inlet gas path 5, the quality and the generating efficiency of micro-nano bubble water are improved, the overall structure of the micro-nano bubble liquid generating system 100 is simple, the use of parts is simplified, the production cost is reduced, the product cost performance is improved, and the experience effect of a user is optimized.
Alternatively, the feed valve 74 and the pressure maintaining valve 72 are connected in series to the feed flow path 7, and two feed flow paths 7 may be provided.
Alternatively, as shown in fig. 1 and 2, both ends of the feed valve 74 and the pressure maintaining valve 72 are connected in parallel and then connected in series to the feed liquid flow path 7, and at this time, the feed valve 74 and the pressure maintaining valve 72 may be connected in sequence through the same feed liquid flow path 7. That is, the upper end of the feed valve 74 and the upper end of the pressure maintaining valve 72 are connected in parallel, the lower end of the feed valve 74 and the lower end of the pressure maintaining valve 72 are connected in parallel, and the feed valve 74 and the pressure maintaining valve 72 connected in parallel are connected in series with the liquid inlet flow path 7.
Further, as in the second aspect example of fig. 4-5, the inlet valve 74 is a two-position three-way valve 75, the two-position three-way valve 75 having two outlet water paths arranged in parallel, and the pressure maintaining valve 72 connected in series to one of the two outlet water paths.
In a particular example, a pressure maintaining valve 72 may be connected in series in the left side outlet water circuit. Thereby simplifying the structure of the micro-nano bubble liquid generating system 100 and reducing the cost. The two-position three-way valve 75 has an AB path or an AC path, as shown in fig. 6, when air needs to be introduced into the mixing chamber 16, the AC path is closed, the AB path is opened, the pressure stabilizing valve 72 is opened, and at this time, the liquid can still be fed into the liquid inlet 12 toward the air dissolving device 1, so that the liquid outlet 13 of the air dissolving device 1 can still output a certain amount of liquid. When the mixing chamber 16 needs to dissolve gas, the AC passage is opened and the AB passage is closed, the inflator 52 stops inflating, at this time, the liquid entering from the AC passage flows into the mixing chamber 16 through the liquid inlet 12, so that the gas space in the mixing chamber 16 is occupied, the pressure of the mixing chamber 16 is increased, and the gas is further promoted to be dissolved in the liquid to form the gas-dissolved liquid.
Still alternatively, in the case where the air intake assembly 50 is only the inflator 52 in the present invention, the liquid path pressure regulating valve assembly 70 is not limited to the water inlet valve 74 and the pressure maintaining valve 72, for example, in the third aspect example in fig. 7 to 8, the liquid path pressure regulating valve assembly 70 includes an adjustable pressure maintaining valve 76, and the adjustable pressure maintaining valve 76 can change its own water flow rate by changing its own internal channel flow cross section or closing its internal channel, so as to adjust the liquid inlet pressure of the liquid inlet 12.
As shown in fig. 9, when the air dissolving device 1 needs to intake air, the adjustable pressure stabilizing valve 76 adjusts the pressure thereof to P1, so as to output a smaller flow rate, and gradually enlarge the space for accommodating air in the mixing chamber 16, thereby facilitating the air filling of the inflator 52 into the mixing chamber 16; when the air dissolving device 1 needs to dissolve air, the adjustable pressure stabilizing valve 76 adjusts the pressure to be P1-P2, and P2 is greater than P1, so that the space for accommodating air in the mixing cavity 16 is gradually reduced, and the pressure in the mixing cavity 16 is increased, so that the air is quickly dissolved in liquid to form air-dissolved liquid.
Advantageously, the air pressure pumped by inflator 52 is not less than the lower threshold of the adjustable pressure range of adjustable pressure maintaining valve 76. That is, the air pressure pumped by inflator 52 is greater than or equal to the lower threshold of the adjustable pressure range of adjustable pressure maintaining valve 76. Therefore, after the water pressure is reduced, air can be pumped into the mixing cavity 16, the water inlet does not need to be turned off, and the use feeling of a user is improved.
Advantageously, the upper threshold of the adjustable pressure range of adjustable pressure maintaining valve 76 is greater than the value of the air pressure pumped by inflator 52. That is, the amount of air pressure pumped by inflator 52 is less than the upper threshold of the adjustable pressure range of adjustable pressure stabilizing valve 76. Thus, it is avoided that the air pressure pumped by the inflator 52 is too high to feed water into the mixing chamber 16.
It should be noted here that the adjustable pressure stabilizing valve 76 can adjust the pressure stabilizing range, which is generally between 0.05MPa and 0.5 MPa.
Optionally, the adjustable pressure stabilizing valve 76 may be two-stage pressure regulating, the adjustable pressure stabilizing valve 76 may also be multi-stage pressure regulating, and the adjustable pressure stabilizing valve 76 may also be stepless pressure regulating. Therefore, the water inlet pressure can be conveniently adjusted, and the use is convenient.
Of course, the adjustable pressure maintaining valve 76 of the present invention may be disposed at the front end of the liquid inlet 12 together with the water inlet valve 74 instead of the conventional pressure maintaining valve 72 described above.
Alternatively, in the case where the air intake assembly 50 of the present invention is the inflator 52, the pressure regulating valve assembly 70 is not limited to the intake valve 74 and the pressure maintaining valve 72, and as shown in the fourth example of fig. 12 to 13, the pressure regulating valve assembly 70 includes: the pressure regulating valve 77 is connected in series to the liquid inlet flow path 7, and the outlet water pressure of the pressure regulating valve 77 is adjustable between an upper threshold and a lower threshold. That is to say, the liquid inlet flow path 7 is connected in series with the pressure regulating valve 77, the pressure regulating valve 77 has an upper threshold and a lower threshold, and the pressure regulating valve 77 can be regulated between the upper threshold and the lower threshold, so that the water inlet pressure is not less than the lower threshold and not greater than the upper threshold, the water inlet pressure is convenient to regulate, the air is easily inflated into the air dissolving device 1 when the water inlet pressure is reduced, and the content of micro-nano bubbles in water can be increased when the water inlet pressure is increased. As shown in fig. 14, when air needs to be supplied into the mixing chamber 16, the pressure regulating valve 77 is switched from the high-pressure position to the low-pressure position, so that the water outlet pressure is at the lower threshold value, and the liquid in the liquid inlet 12 enters the air dissolving device 1 at a small flow rate, at which time the air pump 52 is turned on and inflates air into the mixing chamber 16, so that the mixing chamber 16 is filled with the required air; when gas needs to be dissolved in the mixing chamber 16, the pressure regulating valve 77 is switched from a low-pressure gear to a high-pressure gear, so that the water outlet pressure is an upper valve value, the liquid entering the gas dissolving device 1 from the liquid inlet 12 is large in flow, at the moment, the inflator 52 is closed, and under the condition that the liquid in the mixing chamber 16 is continuously increased, the pressure in the mixing chamber 16 is increased, so that the gas is dissolved in the liquid to form gas-dissolved liquid.
In some embodiments of the present invention, as shown in the first aspect example in fig. 1 to 2, the second aspect example in fig. 4 to 5, the third aspect example in fig. 7 to 8, the fourth aspect example in fig. 12 to 13, the sixth aspect example in fig. 19, 20, 21, and the eighth aspect example in fig. 26, 27, and 28, the liquid outlet 13 is formed at the bottom of the gas dissolving device 1, the liquid inlet 12 is formed at the top or upper portion of the gas dissolving device 1, and the gas inlet 11 is formed at the top, bottom, or side wall of the gas dissolving device 1. That is to say, the air inlet 11 may be formed at the top of the air dissolving device 1, the air inlet 11 may also be formed at the bottom of the air dissolving device 1, the air inlet 11 may also be formed at the side wall of the air dissolving device 1, the liquid inlet 12 may be formed at the top of the air dissolving device 1, the liquid inlet 12 may also be formed at the upper part of the air dissolving device 1, and the liquid outlet 13 is formed at the bottom of the air dissolving device 1. Therefore, different use scenes can be met according to different user requirements, and the method is flexible and convenient.
As shown in fig. 11, the liquid inlet 12 is formed at the top of the air dissolving device 1, and can increase the flow velocity of water flow and increase the air bubble content of the air bubble mixed flow; the air inlet 11 is formed at the top of the air dissolving device 1, so that the structure is simple and the assembly is convenient; the liquid outlet 13 is formed in the bottom of the gas dissolving device 1, and by utilizing the gravity of water and the pressure in the gas dissolving device 1, the water can smoothly flow out without additionally arranging parts, water does not stay for a long time, the water quality is influenced, and the human health is damaged.
In other examples, it is also not limited to providing the liquid inlet 12 and the gas inlet 11 on the air dissolving device 1, and as shown in the fifth aspect example in fig. 16-17, the seventh aspect example in fig. 22, 23 and 24, and the ninth aspect example in fig. 29, 30 and 31, the liquid inlet 12 and the gas inlet 11 may be combined into a merging port 82 to communicate with the mixing chamber 16 of the air dissolving device 1. Therefore, in these examples, either the intake liquid or the intake air flows into the mixing chamber 16 through the merging opening 82, so that the opening required to be formed in the air dissolving device 1 is saved, the sealing performance of the air dissolving device 1 is improved, and the structure of the air dissolving device 1 is simplified.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes: and the controller 3 is in communication connection with the inflator 52 and is used for controlling the inflator 52 to start and stop, so as to control the inflator 52 to supply air to the mixing chamber 16 after being started, or control the inflator 52 to stop supplying air to the mixing chamber 16 after being stopped. Alternatively, the controller 3 is connected to the pump body 53 of the air intake assembly 50 for controlling the start and stop of the pump body 53, so as to control the pump body 53 to pump liquid and promote air intake in the mixing chamber 16 when opened, and control the pump body 53 to control dissolved air in the mixing chamber 16 when closed. Through the effect of controller 3, can simplify the operating procedure of micro-nano bubble liquid generation system 100, reduce the operation degree of difficulty, convenient to use, intelligent degree height.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes: the water flow sensor 71 and the water flow sensor 71 are disposed on the liquid inlet flow path 7 to detect the liquid inlet flow rate of the liquid inlet flow path 7, so that whether liquid flows through and the flow rate of the liquid flowing through can be detected in real time. The water flow sensor 71 is in communication connection with the controller 3, so that the controller 3 can accurately control the water inflow and the water inflow pressure in the mixing chamber 16, resources are saved, and sufficient liquid can be ensured to meet dissolved air.
As in the examples shown in fig. 3, 6, 9, 14, 18, the controller 3 is configured to control activation of the inflator 52 to inflate when the water flow signal is detected by the water flow sensor 71. As in the example shown in fig. 25, 32, the controller 3 is configured to control the pump body 53 to start pumping when the water flow sensor 71 detects a water flow signal. Thereby enabling the controller 3 to control the inflator 52 or the pump body 53 to perform air intake in the mixing chamber 16 when the water flow sensor 71 detects a water flow signal.
In order to further improve the control necessity of air intake, the micro-nano bubble liquid generation system 100 further includes a water outlet switch 61, the water outlet switch 61 is disposed on the water outlet flow path 6 of the air dissolving device 1, the water outlet switch 61 is in communication connection with the controller 3, and when the water outlet switch 61 is opened, the controller 3 controls the mixing chamber 16 to be in an air intake state. That is, when the water outlet switch 61 is turned on, it indicates that the water end connected to the water outlet flow path 6 needs to use water, and at this time, the liquid will pass through the liquid inlet flow path 7, so that when the water flow sensor 71 detects that the liquid passes through, the controller 3 can control the pump body 53 or the inflator 52 to operate, and the air inlet path 5 is promoted to inlet air into the mixing chamber 16.
Alternatively, the water flow sensor 71 is provided downstream of the liquid path pressure regulating valve assembly 70 in the direction of water flow, for example, on the inlet flow path 7 and in front of the inlet 12; for example, the flow path is provided on the junction channel 8 and in front of the junction 82. Alternatively, the water flow sensor 71 is provided upstream of the liquid passage pressure regulating valve assembly 70 in the water flow direction. Therefore, the installation of a user is facilitated according to different requirements, the operation is convenient, and the application range is enlarged.
In other examples, the water flow sensor 71 may be disposed on the liquid outlet flow path 6, wherein in the example where the pump body 53 is disposed on the liquid outlet flow path 6, the pump body 53 is used as a reference, and the water flow sensor 71 may be disposed on the front side of the pump body 53 and on the rear side of the liquid outlet 13; or, the water flow sensor 71 can be arranged on the rear side of the pump body 53 and positioned on the front side of the water outlet switch 61, the arrangement position of the water flow sensor 71 can be flexibly selected according to actual needs, and convenience in installation of a user is improved.
When the air dissolving device 1 is in the process of air dissolving operation for a certain time, the liquid outlet flow path 6 will continuously discharge a certain amount of air dissolving liquid, the water flow sensor 71 will continuously detect the water flow, and the water outlet switch 61 is also continuously in the on state, at this time, the circulation control program can be executed through the further control program, so as to realize liquid discharging and air intake in the middle of operation.
Further, the controller 3 is also in communication connection with the liquid path pressure regulating valve assembly 70 and the air intake assembly 50, respectively, and the controller 3 is configured to control the liquid path pressure regulating valve assembly 70 to switch to the low water pressure state when the accumulated water flow of the water flow sensor 71 is greater than a first preset flow L1 or the accumulated service time of the water flow sensor 71 is greater than a first preset time T4, and the controller 3 controls the air intake assembly 50 to operate to enter the air intake state, so that the liquid discharge and air intake process of the air dissolving device 1 is realized during operation, air in the mixing chamber 16 is supplemented, and the content of gas in the air dissolving liquid is increased. As shown in fig. 18, during the liquid discharge and air intake, the liquid path pressure regulating valve assembly 70 can be controlled to operate at a low water pressure state, i.e., a low water flow operation time T2, and the inflator 52 can be controlled to operate at a low water flow operation time T3, so as to achieve the air intake of the mixing chamber 16.
It should be noted that, here, the control of the operation of the intake assembly 50 includes the operation of controlling the pumping operation of the pump body 53 and/or the operation of controlling the charging operation of the inflator 52, and the control operation may be performed according to the components designed in the respective examples.
Alternatively, after the water outlet switch 61 is turned off, the controller 3 is configured to control the mixing chamber 16 to be in the air inlet state again when the water outlet switch 61 is turned off for a time period longer than a second preset time T5 and the water outlet switch 61 is turned on again, that is, the water flow sensor 71 does not detect that the water flow rate (no water flow signal) is longer than T5 continuously, so that a certain amount of dissolved air liquid is always kept in the mixing chamber 16.
In other examples, when the water outlet switch 61 is turned on again when the water outlet switch 61 is turned off last time and the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2, the controller 3 controls the mixing chamber 16 to be in the air inlet state again, so that the air in the mixing chamber 16 is supplemented.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161, the liquid level sensor 161 is in communication connection with the controller 3, the liquid level sensor 161 is configured to detect a liquid level height of the liquid in the mixing chamber 16, so as to accurately determine the liquid level in the mixing chamber 16, and further determine the pressure in the mixing chamber 16 according to the liquid level, which is beneficial to more accurately determining and controlling a liquid discharge, air intake, and air dissolution process in the mixing chamber 16, so as to further ensure the quality of the air dissolution liquid flowing out from the liquid outlet flow path 6, provide reliable guarantee for the subsequent formation of micro-bubble water, and ensure the air content density of the micro-bubble water.
Optionally, when the liquid level sensor 161 is disposed at a lower position of the mixing chamber 16, when the liquid level sensor 161 detects a water flow signal, the controller 3 enters a liquid discharge and air intake process, at this time, the controller 3 controls the liquid path pressure regulating valve assembly 70 to operate to reduce its water flow, and the controller 3 further controls the pump body 53 to pump liquid to make the air dissolving device 1 intake air.
As shown in fig. 25 and 32, the controller 3 is configured to control the air intake assembly 50 to stop operating when the liquid level is lower than the lower limit of the preset liquid level threshold, in these examples, since the pump body 53 will continuously pump liquid in the early stage, the liquid outlet flow path 6 will continuously discharge dissolved gas liquid outwards, so that the liquid level in the mixing chamber 16 will continuously decrease, the space capable of accommodating the gas volume in the mixing chamber 16 increases, the pressure in the mixing chamber 16 decreases, and the gas in the air intake path 5 will continuously fill the mixing chamber 16, and by controlling the air intake assembly 50 to stop operating, the amount of gas finally filled into the mixing chamber 16 can be controlled, so as to ensure that the gas filled into the mixing chamber 16 is sufficient, and ensure that a certain amount of liquid remains in the mixing chamber 16, thereby effectively preventing the water end from being cut off.
Further optionally, after the air intake of the mixing chamber 16 is completed, the controller 3 is further configured to keep the air intake assembly 50 stopped and control the liquid path pressure regulating valve assembly 70 to switch to a high water pressure state when the liquid level is lower than the lower limit value of the preset liquid level threshold, where the liquid path pressure regulating valve assembly 70 is in a high flow rate state, so that the liquid path pressure regulating valve assembly 70 quickly supplies liquid to the mixing chamber 16, thereby increasing the pressure in the mixing chamber 16 and promoting the gas in the mixing chamber 16 to be dissolved in the liquid as soon as possible. As shown in fig. 25 and 32, in these examples, the pump body 53 is closed, facilitating efficient formation of the liquid solution in the mixing chamber 16. The level sensor 161 in these examples is suitably located at a lower portion of the mixing chamber 16.
Optionally, when the liquid level sensor 161 is disposed at the middle and upper portion of the mixing chamber 16, the controller 3 is configured to control the inflator 52 to inflate the air dissolving device 1 when the liquid level detected by the liquid level sensor 161 is at the preset liquid level height threshold, and the inflation may be performed by discharging liquid and intaking air through the pump body 53, or the inflation may be performed by discharging liquid and intaking air through the pump body 53 and simultaneously inflating high-pressure air through the inflator 52, so as to refill the mixing chamber 16 with the required gas. In the present invention, the requirement for filling gas into the mixing chamber 16 can be determined by determining and detecting the height of the liquid level in the mixing chamber 16.
The preset liquid level height in the invention can be selected and flexibly set according to the actual situation.
In some embodiments of the present invention, the air pressure pumped by inflator 52 is in the range of 0.1MPa to 1.2 MPa; and/or the feed pressure of the feed liquid flow path 7 is in the range of 0.01MPa to 1.2 MPa. That is, it may be that the air pressure pumped by the inflator 52 is in the range of 0.1MPa to 1.2 MPa; or the water inlet pressure of the liquid inlet flow path 7 is in the range of 0.01MPa to 1.2 MPa; the air pressure pumped by the inflator 52 can be in the range of 0.1MPa to 1.2MPa, and the water inlet pressure of the liquid inlet flow path 7 is in the range of 0.01MPa to 1.2 MPa. Therefore, the control logic of the controller 3 is simplified, and the production cost is reduced.
For example, the air pressure pumped by the inflator 52 may be: 0.1MPa, 0.15MPa, 0.2MPa, 0.25MPa, 0.3MPa, 0.35MPa, 0.4MPa, 0.45MPa, 0.5MPa, 0.55MPa, 0.6MPa, 0.65MPa, 0.7MPa, 0.75MPa, 0.8MPa, 0.85MPa, 0.9MPa, 0.95MPa, 1.0MPa, 1.05MPa, 1.1MPa, 1.15MPa, 1.2MPa, etc.
Then, correspondingly, the inlet water pressure of the inlet liquid flow path 7 may be: 0.01MPa, 0.05MPa, 0.1MPa, 0.15MPa, 0.2MPa, 0.25MPa, 0.3MPa, 0.35MPa, 0.4MPa, 0.45MPa, 0.5MPa, 0.55MPa, 0.6MPa, 0.65MPa, 0.7MPa, 0.75MPa, 0.8MPa, 0.85MPa, 0.9MPa, 0.95MPa, 1.0MPa, 1.05MPa, 1.1MPa, 1.15MPa, 1.2MPa and the like.
In some embodiments of the present invention, the liquid inlet 12 is provided with a jet member for jetting a fluid into the gas dissolving device 1, and/or the liquid inlet 12 is provided with a plurality of liquid inlet holes arranged at intervals. That is, the jet member may be positioned at the position of the liquid inlet 12 of the air dissolving device 1 to jet the liquid into the mixing chamber 16, a plurality of liquid inlet holes may be formed at the position of the liquid inlet 12, and the jet member and the plurality of liquid inlet holes may be formed at the position of the liquid inlet 12. Like this, when liquid gets into and dissolves gas device 1, the liquid velocity of flow increases, has improved the area of contact of liquid with the air, makes the air bubble in dissolving gas device 1 denser to micro-nano bubble water provides firm guarantee for follow-up formation.
In the description of the present invention, "a plurality" means two or more unless specifically defined otherwise.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes a micro-nano bubble generator 41, and the micro-nano bubble generator 41 is connected to the liquid outlet flow path 6 of the air dissolving device 1, and is configured to convert the air dissolving liquid into micro-nano bubble water.
Optionally, the micro-nano bubble generator 41 may include a micro-nano bubbler having an axially through micro-nano bubble water micro-channel formed therein, the micro-nano bubble water micro-channel may have a venturi structure, one or more micro-nano bubble water micro-channels may be provided, and the dissolved air water in the bubble water micro-channel is discharged through the micro-nano bubble water micro-channel, so that micro-nano bubble water with high micro-nano bubble density may be generated.
Optionally, a gap water flow channel is arranged in the micro-nano bubble generator 41. Because the water hole size of the micro-nano bubble water micro-channel of the micro-nano bubble generator 41 is small, especially when the water pressure of the inlet water is small, the water outlet amount is small, and the normal water demand of the user is difficult to meet. Therefore, the micro-nano bubble generator 41 may be provided with a gap water passing channel besides the micro-nano bubble water micro-channel, when the water pressure of the inlet water is low, the gap water passing channel may be turned on to increase the water output of the micro-nano bubble generator 41, and when the water pressure of the inlet water is high, the gap water passing channel may be turned off to allow the micro-nano bubble water to flow out of the micro-nano bubble water micro-channel of the micro-nano bubble generator 41.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes a water outlet member 4, the water outlet member 4 is connected to the end of the liquid outlet flow path 6 (i.e. the end of the liquid outlet flow path 6 away from the liquid outlet 13), and the micro-nano bubble generator 41 is disposed in the water outlet member 4, so as to reduce the dissipation of the micro-nano bubbles in the liquid outlet flow path 6, and further improve the quality of the micro-nano bubble water. The water outlet member 4 is directly exposed to the water using end, and the installation and maintenance are convenient.
Optionally, the water outlet 4 is a shower head, for example, the shower head can be a shower head on a kitchen sink in a kitchen, or a shower head of shower water, or a shower head in a dishwasher, so that the micro-nano bubble water flowing out of the water outlet 4 can increase the cleaning effect and the sterilization effect of the outlet. For example, clean cleaning of vegetables, fruits and meat can be realized; but also can realize the clean and clean of the dishes.
Optionally, the water outlet member 4 is a water tap, for example, a water tap on a kitchen sink or a water tap on a wash basin for domestic water, so that the micro-nano bubble water flowing out of the water outlet member 4 can also increase the degradation of the pesticide residue on the vegetables and kill bacteria and viruses.
In some embodiments of the present invention, as shown in fig. 11, the air dissolving device 1 includes: a housing 14 and a partition 15, the housing 14 including: first end cap 141, second end cap 142 and the main cavity body, baffle 15 is located the inside of the main cavity body, be formed with through-hole 151 on the baffle 15, connect the turn-ups and cross the water tank, connect the turn-ups and the internal perisporium welded connection of main cavity body, baffle 15 separates the main cavity body and goes out hybrid chamber 16 and dissolved water chamber, hybrid chamber 16 is located the left side of baffle 15, dissolved water chamber is located the right side of baffle 15, inlet 12 is formed directly over hybrid chamber 16, liquid outlet 13 is formed in the bottom of casing 14, and liquid outlet 13 is formed in the dissolved water chamber below, air inlet 11 is formed at the top of casing 14, the main cavity body is at liquid outlet 13, air inlet 11 and inlet 12 department, all be formed with the avoidance depression towards the internal portion of main cavity, gas dissolving device 1 overall structure is simple, and is convenient for installation and maintenance, low in production cost.
In some embodiments, the ratio between the width dimension of the mixing chamber 16 in the left-right direction and the width dimension of the dissolved water chamber in the left-right direction is in the range of 1/5 to 1. That is, the ratio between the width dimension of the mixing chamber 16 and the width dimension of the dissolved water chamber in the left-right direction is in the range of 1/5 to 1, and when the ratio between the width dimension of the mixing chamber 16 and the width dimension of the dissolved water chamber is less than 1/5, the width dimension of the mixing chamber 16 in the left-right direction is small, and sufficient air bubble mixing cannot be generated in the mixing chamber 16, thereby affecting the bubble content of the dissolved water and the quality of the dissolved water; when the ratio between the width dimension of the mixing cavity 16 and the width dimension of the dissolved water cavity is greater than 1, the width dimension of the mixing cavity 16 in the left-right direction is large, the width dimension of the dissolved water cavity in the left-right direction is small, the air bubbles in the mixing cavity 16 are mixed, the amount of water to be dissolved in the dissolved water cavity is small, and the air bubbles are mixed, so that the water cannot be completely dissolved into water, thereby causing resource waste and affecting the requirement of a user for using the dissolved water.
As shown in fig. 11, in the left-right direction, the ratio between the width of the mixing chamber 16 and the width of the dissolved water chamber is in the range of 1/5 to 1, so that the water flow parallel to the partition 15 is prevented from impacting the partition 15 to influence the generation of air bubble mixed flow, when the water flow impacts to form the air bubble mixed flow, in the mixing chamber 16 with a relatively small space, the air bubbles in the air bubble mixed flow are denser, the micro-nano bubbles have more content, and the quality of the micro-nano bubble water is improved. Therefore, the generated air bubbles are mixed and dissolved into the dissolved water sufficiently, the waste of resources is avoided, and the quality of the dissolved water is ensured.
For example, in the left-right direction, the ratio between the width dimension of the mixing chamber 16 and the width dimension of the dissolved water chamber may be: 1/5, 1/4, 1/3, 1/2, 1, and so forth.
Preferably, as shown in fig. 11, the ratio between the width dimension of the mixing chamber 16 and the width dimension of the dissolved water chamber in the left-right direction is 1/2. Therefore, the sufficient content of micro-nano bubbles in the air bubble mixed flow is ensured, and the economical practicability of the air dissolving device 1 is improved.
In some embodiments, the ratio between the volume of the mixing chamber 16 and the volume of the dissolving water chamber is in the range of 1/4 to 1. When the ratio of the volume of the mixing cavity 16 to the volume of the dissolved water cavity is smaller than 1/4, the volume of the mixing cavity 16 is smaller, the air bubbles generated in the mixing cavity 16 are insufficient in mixing, and the content of the bubbles in the dissolved air liquid cannot be ensured, so that the quality of the dissolved air liquid is reduced, and the user experience is influenced; when the ratio of the volume of the mixing cavity 16 to the volume of the dissolving water cavity is greater than 1, the volume of the mixing cavity 16 is large, the air bubbles in the mixing cavity 16 are mixed more, the liquid to be dissolved in the dissolving water cavity cannot be dissolved into the air bubbles as much as possible, the air bubbles are mixed more, and the waste of resources is caused.
In some specific examples, the ratio between the volume of the mixing chamber 16 and the volume of the dissolved water chamber may be: 1/4, 1/3, 1/2, 1, and so forth.
Optionally, the ratio between the volume of the mixing chamber 16 and the volume of the dissolving water chamber is 1/2. Therefore, the volume capacity of the dissolved water cavity is ensured to be enough for users to use, and the content of micro-nano bubbles in the air bubble mixed flow is ensured to be sufficient, so that the economical practicability of the air dissolving device 1 is improved.
In some embodiments, the ratio of the vertical dimension of the partition 15 to the vertical dimension of the cross-section of the housing 14 at the location of the partition 15 is between 0.4 and 0.9. That is to say, the upper portion or the lower part of baffle 15 and casing 14 interval form and overflow the passageway, and when the ratio between the height dimension of baffle 15 in the up-down direction and the up-down direction size of casing 14 cross baffle 15 position department cross-section was less than 0.4, the air bubble mixed flow can only get into the dissolved water chamber through the through-hole 151 of baffle 15, and the air bubble mixed flow is less, and the air bubble mixed flow is incomplete, inhomogeneous with water, has reduced the content of micro-nano bubble in the micro-nano bubble water to the quality of micro-nano bubble water has been reduced.
When the ratio of the height dimension of the partition 15 in the vertical direction to the dimension of the cross section of the position where the partition 15 is located is larger than 0.9, the distance between the upper side of the partition 15 and the upper end of the shell 14 is large, a large amount of air bubble mixed flow directly enters the dissolved water cavity from the mixing cavity 16 from the overflowing channel at the upper end of the partition 15, so that the air bubble mixed flow in the main cavity is incompletely and unevenly mixed with water, the quantity of micro-nano bubbles in the micro-nano bubble water is reduced, and the quality of the micro-nano bubble water is reduced.
Therefore, the ratio of the height dimension of the partition plate 15 in the vertical direction to the dimension of the cross section of the shell 14 passing through the partition plate 15 in the vertical direction is 0.4-0.9, so that the mixing speed of the air bubble mixed flow and water in the main cavity is accelerated, and the air bubble mixed flow and water are fully mixed.
In a specific example, the ratio of the height dimension of the partition 15 in the up-down direction to the dimension of the cross section of the housing 14 at the position where the partition 15 passes is between 0.4 and 0.9: 0.4, 0.45, 0.5, 0.55, 0.6, 0.65, 0.7, 0.75, 0.8, 0.85, 0.9, etc.
Optionally, the ratio of the height dimension of the partition 15 in the vertical direction to the dimension of the cross section of the shell 14 passing through the partition 15 in the vertical direction is 0.4, so that the quality of the micro-nano bubble water is ensured, the mixing speed of the air bubble mixed flow and the water in the main cavity is increased, and the air bubble mixed flow and the water are mixed fully.
When the water inlet pressure is lower than the air inlet pressure, the liquid inlet 12 of the air dissolving device 1 is closed, the air is pumped into the shell 14 of the air dissolving device 1 through the air inlet 11 by the inflator 52, the water in the air dissolving device 1 is discharged out of the air dissolving device 1 from the liquid outlet 13, the air enters the air dissolving device 1, and the inflator 52 stops supplying the air after the air dissolving device 1 is filled with part or all of the air. Then, the liquid inlet 12 is opened, high-pressure water enters the mixing cavity 16 of the air dissolving device 1 through the liquid inlet 12, in the high-pressure mixing cavity 16, water flow impacts to form air bubble mixed flow, the contact area of air and water is increased, the content of air dissolved in liquid is increased, finally air dissolved liquid is formed, and the air dissolved liquid flows into the water dissolving cavity through the partition plate 15.
In some embodiments of the present invention, the micro-nano bubble liquid generating system 100 further includes a power supply device 2 (the position of the power supply device 2 can be seen in fig. 10, 15, and 40), and the power supply device 2 is connected to the controller 3, so as to supply the controller 3 with the required power, so that the controller 3 can operate normally.
The water heater 1000 according to the embodiment of the invention is described below with reference to the drawings of the specification, and the water heater 1000 may be a gas water heater or an electric water heater, so that the gas dissolving effect and the water outlet cleaning power of the water outlet end of the water heater 1000 are greatly improved.
A water heater 1000 according to an embodiment of the present invention includes: a heating device 400 and the micro-nano bubble liquid generating system 100 in the foregoing aspects of examples.
As shown in fig. 10, 15 and 40, the air dissolving device 1 of the micro-nano bubble liquid generating system 100 is disposed at the water outlet end of the heating device 400. In these examples, the heated hot water in the heating device 400 enters the air dissolving device 1 through the inlet flow path 7, so that the dissolved air liquid flowing out from the outlet flow path 6 also has a higher temperature, and the hot water with a higher temperature is supplied to the outside of the water heater 1000.
As shown in fig. 41 and 42, the micro-nano bubble liquid generating system 100 is connected to the water inlet end of the heating device 400, for example, the heating device 400 shown in fig. 41 may be arranged on the liquid outlet flow path 6, so that the heating device 400 is located at the rear of the air dissolving device 1, and the heating device 400 is also located at the rear of the pump body 53. In these examples, the dissolved air liquid or the micro-nano bubble water formed after passing through the micro-nano bubble liquid generating system 100 is heated by the heating device 400, so as to prevent the high-temperature liquid from impacting the pump body 53, and prolong the service life of the pump body 53. For example, a heating device 400 as shown in fig. 42 may be provided on the merged channel 8, and the heating device 400 may be located between the air dissolving device 1 and the pump body 53. In these examples, the hot water heated by the heating device 400 is re-introduced into the air dissolving device 1, so that the air dissolving liquid with a certain temperature is formed in the air dissolving device 1 and is discharged from the liquid outlet flow path 6.
According to the structure, the water heater 1000 of the embodiment of the invention adopts the micro-nano bubble liquid generating system 100, so that the gas-dissolved liquid can be quickly formed in the water heater 1000, and the gas-dissolved liquid with a certain temperature or the micro-nano bubble water formed by the micro-nano bubble generator 41 is conveyed to the water outlet end of the water heater 1000, so that a user can use the water with required properties in time. The internal pressure of the water heater 1000 is adjusted stably, the operation is stable, the user experience is good, and the product safety is high. The user can install micro-nano bubble liquid generation system 100 to required position as required, promotes the flexibility and the convenience of product installation to the practicality of water heater 1000 has been increased. The high-temperature liquid does not pass through the pump body 53, so that the service life of the pump body 53 is ensured, and the pump body 53 is not impacted by the high-temperature liquid.
Alternatively, the heating device 400 may be a heating liner provided with an electric heating pipe, which is mainly applicable to an electric water heater, and the electric heating pipe heats water in the heating liner.
Alternatively, the heating device 400 may be a combination of a fin heat exchanger and a gas burning source, which is mainly suitable for a gas water heater, wherein the gas heats the fin heat exchanger, and water is heated after flowing out from the fin heat exchanger.
Alternatively, as shown in fig. 10, 15, and 40, the water heater 1000 includes: a cold water inlet channel 200, a hot water outlet channel 300, a heating device 400 and a micro-nano bubble liquid generating system 100.
As shown in fig. 10, 15 and 40, the outlet end of the cold water inlet channel 200 is connected to the inlet end of the heating device 400, the inlet end of the hot water outlet channel 300 is connected to the outlet end of the heating device 400, and the outlet end of the hot water outlet channel 300 is connected to the air dissolving device 1.
Further, a mixing cavity 16 is formed in the air dissolving device 1, a liquid level sensor 161 is arranged in the air dissolving device 1, and the controller 3 is in communication connection with the liquid level sensor 161. An air inlet 11, a liquid inlet 12 and a liquid outlet 13 are formed on the air dissolving device 1, the air inlet 11 is formed at the top of the air dissolving device 1, an air inlet path 5 is connected with the air inlet 11, an inflator pump 52 is connected on the air inlet path 5, the controller 3 is in communication connection with the inflator pump 52, and a one-way valve 51 is connected in series at one side of the air inlet path 5 close to the air dissolving device 1. The liquid inlet 12 is formed at the top of the gas dissolving device 1, the liquid inlet flow path 7 is connected with the liquid inlet 12, the water flow sensor 71 is arranged in the liquid inlet flow path 7, and the controller 3 is in communication connection with the water flow sensor 71. As shown in fig. 10, 15 and 40, the outlet end of the hot water outlet flow channel 300 is connected to the inlet flow path 7. The liquid outlet 13 is formed at the bottom of the gas dissolving device 1, the liquid outlet 13 is connected with the liquid outlet flow path 6, and the water outlet switch 61 is connected in series with the liquid outlet flow path 6. The tail end of the liquid outlet flow path 7 is provided with a water outlet part 4, and the micro-nano bubble generator 41 is positioned in the water outlet part 4.
Optionally, as shown in fig. 10 and fig. 15, the water heater 1000 further includes a water pump 73, the water pump 73 is disposed on the liquid inlet flow path 7 and at the water inlet end of the gas dissolving device 1, and is used for increasing the pressure of the water heater 1000 and for starting the circulation preheating function of the water heater 1000.
In the example shown in fig. 10 and 15, when the water heater 1000 is used and the water inlet pressure is lower than the air inlet pressure, cold water flows into the heating device 400 of the water heater 1000 through the cold water inlet flow channel 200, the cold water is converted into hot water in the heating device 400, the hot water flows into the mixing chamber 16 of the air dissolving device 1 through the hot water outlet flow channel 300 via the liquid inlet flow channel 7 of the micro-nano bubble liquid generating system 100, and the water flow sensor 71 sends a water flow signal to the controller 3. When the liquid level sensor 161 in the air dissolving device 1 detects that the water level in the mixing chamber 16 is higher than the preset water level, a signal is transmitted to the controller 3, the controller 3 controls the inflator 52 to start, and the inflator 52 pumps high-pressure air into the mixing chamber 16. The water flow is mixed with high-pressure air to dissolve the air into the liquid, the air in the air dissolving device 1 is gradually reduced, the air pump 52 continuously or intermittently pumps the air into the air dissolving device 1, and the air pressure in the air dissolving device 1 is kept within a certain range. Therefore, the quality of the micro-nano bubble water is ensured, and the use experience of a user is improved.
When the water inlet pressure is not less than the air inlet pressure, as shown in fig. 10, when cold water flows into the heating device 400 of the water heater 1000 through the cold water inlet flow channel 200, the pressure stabilizing valve 72 and the water pump 73 are opened, the pressure stabilizing valve 72 stabilizes the water inlet pressure, and the water pump 73 is used for increasing the water pressure and improving the air dissolving rate. Therefore, the bubble content of the micro-nano bubble water is further ensured, and the production efficiency of the micro-nano bubble water is improved.
Alternatively, as shown in fig. 15, the liquid passage pressure regulating valve assembly 70 includes a pressure regulating valve 77, and the pressure regulating valve 77 is provided on the liquid inlet flow passage 7 and in front of the heating device 400. When the liquid level sensor 161 in the air dissolving device 1 detects that the water level in the mixing chamber 16 is higher than the preset water level, a signal is transmitted to the controller 3, the controller 3 adjusts the pressure of the pressure regulating valve 77 to the lower threshold value so as to reduce the liquid inlet flow, the controller 3 controls the inflator 52 to start, and the inflator 52 pumps high-pressure air into the mixing chamber 16. The water flow is mixed with the high-pressure air to dissolve the air into the liquid, the air in the air dissolving device 1 is gradually reduced, the air pump 52 continuously or intermittently pumps the air into the air dissolving device 1, and the air pressure in the air dissolving device 1 is kept within a certain range. When the liquid level sensor 161 in the air dissolving device 1 detects that the water level in the mixing chamber 16 is lower than the lower limit value of the preset liquid level height threshold value, the air charging pump 52 is closed, and the pressure of the pressure regulating valve 77 is adjusted to the upper threshold value so as to increase the liquid inlet flow rate of the mixing chamber 16. Like this, guaranteed the quality of micro-nano bubble water, improved user's use and experienced, and at the in-process that admits air and dissolve gas, the water end can not cut off the water all the time.
Alternatively, as shown in fig. 40, referring to the micro-nano bubble liquid generating system 100 shown in the sixth aspect example in fig. 19, 20 and 21, and the eighth aspect example in fig. 26, 27 and 28, the air intake assembly 50 includes an air pump 52 and a pump body 53, wherein the air pump 52 is disposed on the air intake path 5, the pump body 53 is disposed on the liquid outlet path 6, and the liquid path pressure regulating valve assembly 70 and the air dissolving device 1 are both disposed on the water outlet end of the heating device 400.
When the water heater 1000 shown in fig. 40 is in use, the water outlet switch 61 is turned on, the water flow sensor 71 sends a water flow signal to the controller 3, the controller 3 controls the liquid path pressure regulating valve assembly 70 to be in a low water pressure state, and the controller 3 controls the pump body 53 to discharge liquid and controls the inflator 52 to intake air into the mixing chamber 16; when the liquid level sensor 161 in the air dissolving device 1 detects that the water level in the mixing chamber 16 is lower than the lower limit value of the preset liquid level height threshold, the controller 3 controls the pump body 53 to stop discharging liquid and controls the inflator 52 to stop supplying air; at the same time, the controller 3 controls the liquid path pressure regulating valve assembly 70 to be in a high water pressure state so that the liquid inlet flow path 7 feeds a large flow of hot water into the mixing chamber 16, and the pressure in the mixing chamber 16 is increased to form a high-pressure dissolved gas liquid. Therefore, the required gas-dissolved liquid is conveyed to the water outlet part 4 by the liquid outlet flow path 6 of the mixing cavity 16, and the gas-dissolved liquid forms micro-nano bubble water with a certain temperature in the micro-nano bubble generator 41 of the water outlet part 4 and is output outwards for use by a user.
Optionally, the water heater 1000 comprises: a cold water inlet flow passage 200, a hot water outlet flow passage 300, a heating device 400 as shown in fig. 41, and a micro-nano bubble liquid generating system 100 as shown in the examples of the seventh aspect in fig. 22 to 24, and the ninth aspect in fig. 29 to 31. Wherein, the liquid outlet flow path 7 of the air dissolving device 1 is connected to the cold water inlet flow path 200 and is located at the water inlet end of the heating device 400. The water outlet end of the heating device 400 is connected with a hot water outlet flow passage 300, the hot water outlet flow passage 300 is connected with the other section of the water outlet flow passage 7 and is connected with the water outlet member 4, and a water outlet switch 61 is arranged on one side of the water outlet flow passage 7 close to the water outlet member 4. In these examples, the dissolved gas liquid with a low temperature is formed in the gas dissolving device 1, and then the dissolved gas liquid is sent to the heating device 400 to be heated, so as to form the dissolved gas liquid with a high temperature, and the dissolved gas liquid is output to the water outlet member 4. Therefore, the pump body 53 of the present invention is not impacted by hot water, and the service life of the pump body 53 is prolonged.
Optionally, the water heater 1000 comprises: a cold water inlet flow passage 200, a hot water outlet flow passage 300, a heating device 400 as shown in fig. 42, and a micro-nano bubble liquid generating system 100 as shown in the examples of the seventh aspect in fig. 22 to 24, and the ninth aspect in fig. 29 to 31. The converging flow path 8 is connected to the cold water inlet flow path 200 at the water inlet end of the heating device 400, the water outlet end of the heating device 400 is connected to the hot water outlet flow path 300, the hot water outlet flow path 300 is connected to the liquid inlet 12 of the air dissolving device 1, the air dissolving device 1 is connected to the liquid outlet flow path 7 and connected to the water outlet member 4, and a water outlet switch 61 is arranged on one side of the liquid outlet flow path 7, which is close to the water outlet member 4. In these examples, the liquid passing through the pump body 53 enters the heating device 400 to be heated, and the heated fluid enters the air dissolving device 1, so that the air dissolving liquid with a certain temperature is formed in the air dissolving device 1, and the air dissolving liquid is output to the water outlet member 4 through the liquid outlet flow path 6. Therefore, the pump body 53 of the present invention is not impacted by hot water, and the service life of the pump body 53 is prolonged.
The micro-nano bubble liquid generating system 100 of the present invention may be used not only in the water heater 1000 described above, but also in other household appliances, such as a cosmetic instrument or a dishwasher, so that the micro-nano bubble liquid generating system 100 of the present invention has a wider application range.
The following describes a specific structure and a control method of the micro-nano bubble liquid generation system 100 according to an embodiment of the present invention with reference to the drawings. The embodiments of the present invention may be all embodiments obtained by combining the foregoing technical solutions, and are not limited to the following specific embodiments, which fall within the scope of the present invention.
Example 1
A micro-nano bubble liquid generation system 100, comprising: the air dissolving device 1, the water flow sensor 71, the liquid path pressure regulating valve assembly 70, the air inlet assembly 50, the power supply device 2, the controller 3, the water outlet switch 61, the water outlet part 4 and the micro-nano bubble generator 41.
As shown in fig. 1, a mixing chamber 16 is formed in the air dissolving device 1, and an air inlet path 5, an air inlet flow path 7 and an air outlet flow path 6 communicated with the mixing chamber 16 are formed on the air dissolving device 1. The water flow sensor 71 is provided on the intake flow path 7, and the water flow sensor 71 is provided on the intake side of the liquid path pressure regulating valve assembly 70. The liquid path pressure regulating valve assembly 70 is provided in the liquid inlet flow path 7, the liquid path pressure regulating valve assembly 70 is used for regulating the pressure of the liquid inlet flow path 7, and the liquid path pressure regulating valve assembly 70 has a large water pressure state and a small water pressure state. The power supply device 2 supplies power to the controller 3. The water outlet switch 61 is arranged on the water outlet flow path 6 near the water outlet member 4, and the micro-nano bubble generator 41 is arranged in the water outlet member 4.
The pressure regulating valve assembly 70 includes a pressure maintaining valve 72 and a water inlet valve 74 arranged in parallel. The air intake assembly 50 includes an inflator 52 and a check valve 51 provided on the air intake path 5, and the check valve 51 is provided between the inflator 52 and the air dissolving device 1. The controller 3 is in communication with a water flow sensor 71, an inflator 52, a pressure maintaining valve 72 and a water inlet valve 74, respectively.
As shown in fig. 3, when the micro-nano bubble liquid generating system 100 is used, after the water outlet switch 61 is opened by a user, a water flow signal is sent by a water flow sensor 71 and transmitted to the controller 3, the controller 3 supplies power or a signal to the water inlet valve 74, and controls the water inlet valve 74 to close the pressure stabilizing valve 72 and open the pressure regulating valve assembly 70, so that the liquid path pressure regulating valve assembly 70 is in a low water pressure state. Controller 3 controls the operation time T1 of inflator 52, and inflator 52 passes through check valve 51 to discharge water in mixing chamber 16 from liquid outlet 13, and air enters mixing chamber 16 to charge mixing chamber 16. After part or all of the air exists in the mixing chamber 16, the inflator 52 is controlled to stop running, the water inlet valve 74 is controlled to be opened to enable the liquid path pressure regulating valve assembly 70 to be in a high water pressure state, at the moment, the air in the mixing chamber 16 is dissolved in the liquid, so that dissolved air liquid is generated, and when the dissolved air liquid flows out of the water outlet member 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet member 4, so that micro-nano bubble water is generated and is used by a user.
Example 2
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in FIG. 2, a water flow sensor 71 is provided on the outlet side of the inlet valve 74 and the pressure maintaining valve 72. The micro-nano bubble liquid generating system 100 can be used in the manner described in example 1.
Example 3
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 4, the water inlet valve 74 is replaced by a two-position three-way valve 75, the two-position three-way valve 75 has two water outlet paths, the two water outlet paths are respectively communicated with an AB path or an AC path in the two-position three-way valve 75, the AB path and the AC path are connected in parallel, and the pressure maintaining valve 72 is connected in series with the water outlet path communicated with the AB path. The water flow sensor 71 is provided on the water inlet side of the two-position three-way valve 75.
As shown in fig. 6, when the micro-nano bubble liquid generating system 100 is used, after the water outlet switch 61 is opened by a user, a water flow signal is sent by the water flow sensor 71 and transmitted to the controller 3, the controller 3 supplies power or a signal to the two-position three-way valve 75, controls the two-position three-way valve 75AC passage to be closed and controls the AB passage of the two-position three-way valve 75 to be opened, so that the liquid passage pressure regulating valve assembly 70 is in a low water pressure state. Then, the operation time T1 of the inflator 52 is controlled, the inflator 52 discharges the water in the mixing chamber 16 from the liquid outlet after passing through the check valve 51, the air enters the mixing chamber 16, after part or all of the air exists in the mixing chamber 16, the inflator 52 is controlled to stop operating, the AC path of the two-position three-way valve 75 is controlled to be opened, the AB path of the two-position three-way valve 75 is closed to enable the liquid path pressure regulating valve assembly 70 to be in a high water pressure state, the air in the mixing chamber 16 is dissolved in the liquid at this time, so that dissolved air liquid is generated, and when the dissolved air liquid flows out from the water outlet member 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet member 4, so that micro-nano bubble water is generated for the user to use. The water outlet pressure of the pressure stabilizing valve 72 is P1, the air outlet pressure of the inflator 52 is P2, and P2 is more than or equal to P1.
When the dissolved gas liquid in the gas dissolving device 1 needs to be replenished halfway, the controller 3 can control the actions of all the components again to make the mixing cavity 16 intake and discharge gas and dissolve gas under high pressure, thereby forming circulation control until the water outlet switch 61 is closed.
Example 4
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 3, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 5, the water flow sensor 71 is provided between the water outlet side of the two-position three-way valve 75 and the air dissolving device 1. The micro-nano bubble liquid generating system 100 can be used in the manner described in example 3.
Example 5
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 7, the water inlet valve 74 is disabled, the pressure maintaining valve 72 is an adjustable pressure maintaining valve 76, and the water flow sensor 71 is arranged on the water inlet side of the adjustable pressure maintaining valve 76.
As shown in fig. 9, when the micro-nano bubble liquid generating system 100 is used, after the water outlet switch 61 is turned on by a user, a water flow signal is sent by the water flow sensor 71 and transmitted to the controller 3, the controller 3 supplies power or a signal to the adjustable pressure stabilizing valve 76, and controls the water outlet pressure of the adjustable pressure stabilizing valve 76 to be P1, so that the adjustable pressure stabilizing valve 76 is in a low water pressure state. Controller 3 controls the operation time T1 of inflator 52, and inflator 52 passes through check valve 51 to discharge water in mixing chamber 16 from liquid outlet 13, and air enters mixing chamber 16 to charge mixing chamber 16. After part or all of the air exists in the mixing cavity 16, the inflator 52 is controlled to stop running, the water outlet pressure of the adjustable pressure stabilizing valve 76 is controlled to be P1-P2, the adjustable pressure stabilizing valve 76 is in a high water pressure state, the air in the mixing cavity 16 is dissolved in the liquid at the moment, so that air-dissolved liquid is generated, and when the air-dissolved liquid flows out of the water outlet piece 4, the air-dissolved liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that the micro-nano bubble water is generated for a user to use.
Example 6
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 5, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 12, a water flow sensor 71 is arranged between the water outlet side of the adjustable pressure maintaining valve 76 and the air dissolving device 1. The micro-nano bubble liquid generating system 100 can be used in the manner of example 5.
Example 7
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 12, the pressure maintaining valve 72 and the water inlet valve 74 in the liquid passage pressure regulating valve assembly 70 are replaced with a pressure regulating valve 77. The water flow sensor 71 is provided on the water inlet side of the pressure regulating valve 77. The outlet water pressure of the pressure regulating valve 77 is adjustable between an upper threshold and a lower threshold.
As shown in fig. 14, when the micro-nano bubble liquid generating system 100 is used, after the user opens the water outlet switch 61, the water flow sends a water flow signal to the controller 3 through the water flow sensor 71, and the controller 3 supplies power to the pressure regulating valve 77 or signals the pressure of the pressure regulating valve 77 to be a lower threshold value, so as to enter a low water pressure state. Controller 3 controls the operation time T1 of inflator 52, and inflator 52 passes through check valve 51 to discharge water in mixing chamber 16 from liquid outlet 13, and air enters mixing chamber 16 to charge mixing chamber 16. After part or all of the air exists in the mixing cavity 16, the inflator 52 is controlled to stop running, the water outlet pressure of the pressure regulating valve 77 is controlled to be an upper threshold value, the adjustable pressure stabilizing valve 76 is in a high water pressure state, the air in the mixing cavity 16 is dissolved in the liquid at the moment, so that the air-dissolved liquid is generated, and when the air-dissolved liquid flows out of the water outlet piece 4, the air-dissolved liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that the micro-nano bubble water is generated for a user to use.
Example 8
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 7, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 13, the water flow sensor 71 is provided between the water outlet side of the pressure regulating valve 77 and the air dissolving device 1. The micro-nano bubble liquid generating system 100 can be used in the manner described in example 7.
Example 9
A micro-nano bubble liquid generating system 100, which has the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the differences are only that: as shown in fig. 16, the liquid passage pressure regulating valve assembly 70 employs a flow rate regulating valve 78, and the pressure maintaining valve 72 and the flow rate regulating valve 78 are provided in parallel on the liquid inlet flow passage 7. The flow regulating valve 78 may be a flow valve with a continuously adjustable opening or a flow switching valve with a variable multi-gear output flow. The pressure stabilizing valve 72 and the flow regulating valve 78 are connected in parallel and then communicated to the gas dissolving device 1 through the liquid inlet 12. The tail end of the air inlet path 5 is connected to the air dissolving device 1 through an air inlet 11. The water flow sensor 71 is provided on the intake flow path 7 on the intake side of the liquid path regulator valve assembly 70 and the pressure regulator valve 72.
As shown in fig. 18, when the micro-nano bubble liquid generating system 100 is used, after the water outlet switch 61 is opened by a user, a water flow signal is sent by a water flow sensor 71 and is transmitted to the controller 3, the controller 3 supplies power or signals to the flow regulating valve 78 and the pressure stabilizing valve 72, so that the flow regulating valve 78 outputs a small flow, and the pressure stabilizing valve 72 is opened or closed according to actual conditions, so that the liquid path pressure regulating valve assembly 70 enters a small water pressure state. Controller 3 controls the operation time T3 of inflator 52, and inflator 52 passes through check valve 51 to discharge water in mixing chamber 16 from liquid outlet 13, and air enters mixing chamber 16 to charge mixing chamber 16. After part or all of the air exists in the mixing chamber 16, the inflator 52 is controlled to stop running, the flow regulating valve 78 and the pressure stabilizing valve 72 are controlled to act, the flow regulating valve 78 outputs a large flow, so that the liquid path pressure regulating valve assembly 70 enters a large water pressure state, the air in the mixing chamber 16 is dissolved in the liquid at the moment, so that air-dissolved liquid is generated, and when the air-dissolved liquid flows out from the water outlet piece 4, the air-dissolved liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated for a user to use.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 in an accumulated manner, or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4 in an accumulated manner, the flow regulating valve 78, the pressure stabilizing valve 72 and the inflator 52 are controlled to work again, so that the mixing chamber 16 discharges and admits the liquid and the high-pressure dissolved air.
Example 10
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 9, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 17, the water flow sensor 71 is provided between the water outlet side of the flow rate regulating valve 78 and the pressure maintaining valve 72 and the merging port 82, the pressure maintaining valve 72 and the flow rate regulating valve 78 are connected in parallel and then communicated to the air dissolving device 1 through the merging port 82, and the end of the air intake passage 5 is connected to the liquid inlet flow path 7 in front of the merging port 82. The micro-nano bubble liquid generating system 100 can be used in the manner described in example 9.
Example 11
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 1, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 19, the liquid passage pressure regulating valve assembly 70 is provided in the liquid inlet passage 7 by using only the flow rate regulating valve 78. The water flow sensor 71 is provided on the water inlet side of the flow regulating valve 78. The flow rate adjusting valve 78 selects a flow rate switching valve whose multi-stage output liquid flow rate output is variable, and the structure of the flow rate switching valve can be seen in fig. 33 and 34. Further, the intake assembly 50 includes a pump body 53 provided on the liquid outlet flow path 6.
As shown in fig. 25, when the micro-nano bubble liquid generating system 100 is used, after the user opens the water outlet switch 61, the water flow sends a water flow signal to the controller 3 through the water flow sensor 71, and the controller 3 supplies power or a signal to the flow switching valve, so that the flow switching valve enters a low water pressure state and outputs a low flow. The controller 3 controls the pump body 53 to operate, the pump body 53 pumps water in the mixing cavity 16 out from the liquid outlet 13, and gas in the gas inlet path 5 enters the mixing cavity 16, so that the mixing cavity 16 completes gas inlet. After sufficient gas exists in the mixing cavity 16, the pump body 53 is controlled to stop running, the flow switching valve is controlled to enter a high water pressure state and output a large flow, air in the mixing cavity 16 is dissolved in liquid at the moment, so that dissolved air liquid is generated, and when the dissolved air liquid flows out from the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated and is used by a user. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 is drained and filled with water during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow rate is greater than T5 in the water flow sensor 71 for a continuous time, or the controller 3 determines that the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2 in the last operation process, the controller 3 turns on the water outlet switch 61 again, and controls the mixing cavity 16 to be in the air inlet state again, so that a certain amount of air-dissolved liquid is always kept in the mixing cavity 16.
Example 12
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 11, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 26, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. A level sensor 161 is communicatively connected to the controller 3, the level sensor 161 being adapted to detect a level of the liquid in the mixing chamber 16, the level sensor 161 being disposed at a lower portion of the mixing chamber 16.
As shown in fig. 32, when the micro-nano bubble liquid generating system 100 is used, after the user opens the water outlet switch 61, the water flow sends a water flow signal to the controller 3 through the water flow sensor 71, and the controller 3 supplies power or a signal to the flow switching valve, so that the flow switching valve enters a low water pressure state and outputs a low flow. The controller 3 controls the pump body 53 to operate, the pump body 53 pumps water in the mixing cavity 16 out from the liquid outlet 13, and gas in the gas inlet path 5 enters the mixing cavity 16, so that the mixing cavity 16 completes gas inlet. When the liquid level sensor 161 detects that the liquid level in the mixing chamber 16 is lower than the lower limit value of the preset liquid level height threshold, sufficient gas is stored in the mixing chamber 16, the pump body 53 is controlled to stop running, the flow switching valve is controlled to enter a high-water-pressure state and output a large flow, at the moment, the air in the mixing chamber 16 is dissolved in the liquid, so that dissolved air liquid is generated, and when the dissolved air liquid flows out from the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated to be used by a user. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 is drained and filled with water during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow rate is greater than T5 in the water flow sensor 71 for a continuous time, or the controller 3 determines that the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2 in the last operation process, the controller 3 turns on the water outlet switch 61 again, and controls the mixing cavity 16 to be in the air inlet state again, so that a certain amount of air-dissolved liquid is always kept in the mixing cavity 16.
Example 13
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 11, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 20, the micro-nano bubble liquid generating system 100 further includes a pressure stabilizing valve 72, the pressure stabilizing valve 72 is connected in parallel with the flow regulating valve 78 through a liquid separating flow path 81 on the liquid inlet flow path 7, and a liquid outlet end of the liquid separating flow path 81 is arranged on the liquid inlet flow path 7 in front of the liquid inlet 12.
As shown in fig. 25, when the micro-nano bubble liquid generating system 100 is used, after a user opens the water outlet switch 61, water flow sends a water flow signal to the controller 3 through the water flow sensor 71, the controller 3 supplies power or signals to the flow switching valve and the pressure stabilizing valve 72, so that the flow switching valve enters a low water pressure state and outputs a low flow, and the pressure stabilizing valve 72 performs opening and closing control according to actual system pressure. The controller 3 controls the pump body 53 to operate, the pump body 53 pumps water in the mixing cavity 16 out from the liquid outlet 13, and gas in the gas inlet path 5 enters the mixing cavity 16, so that the mixing cavity 16 completes gas inlet. When sufficient gas is filled in the mixing cavity 16, the flow switching valve is controlled to enter a high water pressure state and output a large flow, and the pressure stabilizing valve 72 is controlled to open and close according to the actual system pressure, so that the pressure in the mixing cavity 16 is increased, and air is dissolved in liquid to generate gas-dissolved liquid. When the dissolved air liquid flows out of the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated for a user to use. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 is drained and filled with water during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow rate is greater than T5 in the water flow sensor 71 for a continuous time, or the controller 3 determines that the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2 in the last operation process, the controller 3 turns on the water outlet switch 61 again, and controls the mixing cavity 16 to be in the air inlet state again, so that a certain amount of air-dissolved liquid is always kept in the mixing cavity 16.
Example 14
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 11, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 27, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. A level sensor 161 is communicatively connected to the controller 3, the level sensor 161 being adapted to detect a level of liquid in the mixing chamber 16, the level sensor 161 being disposed at an upper position of the mixing chamber 16.
When the micro-nano bubble liquid generating system 100 is used, after a user opens the water outlet switch 61, water flow sends a water flow signal to the controller 3 through the water flow sensor 71, the controller 3 supplies power or signals to the flow switching valve and the pressure stabilizing valve 72, so that the flow switching valve enters a low water pressure state and outputs a low flow, and the pressure stabilizing valve 72 is opened and closed according to actual system pressure. When the liquid level detected by the liquid level sensor 161 is at the preset liquid level threshold, the controller 3 controls the pump body 53 to operate, the pump body 53 pumps water in the mixing chamber 16 out from the liquid outlet 13, so that gas in the gas inlet path 5 enters the mixing chamber 16, and the mixing chamber 16 completes gas inlet. Until the liquid level is out of the preset liquid level height threshold, sufficient gas is filled in the mixing cavity 16 at the moment, the pump body 53 is controlled to stop running, the flow switching valve is controlled to enter a high-water-pressure state and output a large flow, and meanwhile, the pressure stabilizing valve 72 is controlled to be opened and closed according to the actual system pressure, so that the pressure in the mixing cavity 16 is increased, and air is dissolved in liquid to generate gas-dissolved liquid. When the dissolved air liquid flows out of the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated for a user to use. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 is drained and filled with water during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow rate is greater than T5 in the water flow sensor 71 for a continuous time, or the controller 3 determines that the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2 in the last operation process, the controller 3 turns on the water outlet switch 61 again, and controls the mixing cavity 16 to be in the air inlet state again, so that a certain amount of air-dissolved liquid is always kept in the mixing cavity 16.
Example 15
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 13, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 21, the liquid outlet end of the liquid separation flow path 81 is provided on the liquid outlet flow path 6 and between the pump body 53 and the liquid outlet 13. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 13.
Example 16
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 15, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 28, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. A level sensor 161 is communicatively connected to the controller 3, the level sensor 161 being configured to detect a level of the liquid in the mixing chamber 16, the level sensor 161 being disposed at an upper or lower position of the mixing chamber 16. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 14.
Example 17
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 13, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 22, the pump body 53 is connected to the merging port 82 of the air dissolving device 1 through the merging channel 8, and one end of the merging channel 8 is connected to both the intake channel 7 and the intake air path 5.
As shown in fig. 25, when the micro-nano bubble liquid generating system 100 is used, after a user opens the water outlet switch 61, water flow sends a water flow signal to the controller 3 through the water flow sensor 71, the controller 3 supplies power or signals to the flow switching valve and the pressure stabilizing valve 72, so that the flow switching valve enters a low water pressure state and outputs a low flow, and the pressure stabilizing valve 72 performs opening and closing control according to actual system pressure. The controller 3 controls the pump body 53 to operate, the pump body 53 pumps the liquid in the liquid inlet flow path 7 into the gas dissolving device 1, the air pressure in the merging flow path 7 and the liquid inlet flow path 7 is lower than the air pressure in the gas inlet path 5, so that the gas in the gas inlet path 5 enters the mixing cavity 16 through the merging flow path 7, and the gas inlet of the mixing cavity 16 is completed. When sufficient gas is filled in the mixing cavity 16, the flow switching valve is controlled to enter a high-water-pressure state and output a large flow, and the pressure stabilizing valve 72 is controlled to be opened and closed according to the actual system pressure, so that the pressure in the mixing cavity 16 is increased, and air is dissolved in liquid to generate gas-dissolved liquid. When the dissolved air liquid flows out of the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated for a user to use. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the water flow sensor 71 detects that the water flow is larger than the first preset flow L1 or the accumulated service time of the water flow sensor 71 is larger than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 is drained and filled with water during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow rate is greater than T5 in the water flow sensor 71 for a continuous time, or the controller 3 determines that the accumulated water flow rate of the water flow sensor 71 is greater than the second preset flow rate L2 in the last operation process, the controller 3 turns on the water outlet switch 61 again, and controls the mixing cavity 16 to be in the air inlet state again, so that a certain amount of air-dissolved liquid is always kept in the mixing cavity 16.
Example 18
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 17, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 29, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. The liquid level sensor 161 is connected to the controller 3 in a communication manner, the liquid level sensor 161 is used for detecting the liquid level height of the liquid in the mixing chamber 16, and the liquid level sensor 161 is arranged at the middle position of the mixing chamber 16.
When the micro-nano bubble liquid generation system 100 is used, after a user opens the water outlet switch 61, water flow sends a water flow signal to the controller 3 through the water flow sensor 71, the controller 3 supplies power or signals to the flow switching valve and the pressure stabilizing valve 72, so that the flow switching valve enters a low water pressure state and outputs a low flow, and the pressure stabilizing valve 72 is opened and closed according to actual system pressure. When the liquid level detected by the liquid level sensor 161 is at the preset liquid level threshold, the controller 3 controls the pump body 53 to operate, the pump body 53 pumps the liquid in the liquid inlet flow path 7 into the air dissolving device 1, the air pressure in the converging flow path 7 and the liquid inlet flow path 7 is lower than the air pressure in the air inlet path 5, so that the air in the air inlet path 5 enters the mixing cavity 16 through the converging flow path 7, and the air inlet of the mixing cavity 16 is completed. When sufficient gas is filled in the mixing cavity 16, the liquid level height detected by the liquid level sensor 161 is out of the preset liquid level height threshold value, the flow switching valve is controlled to enter a high-water-pressure state and output a large flow, and meanwhile, the pressure stabilizing valve 72 is controlled to be opened and closed according to the actual system pressure, so that the pressure in the mixing cavity 16 is increased, and air is dissolved in the liquid to generate the gas-dissolved liquid. When the dissolved air liquid flows out of the water outlet piece 4, the dissolved air liquid passes through the micro-nano bubble generator 41 in the water outlet piece 4, so that micro-nano bubble water is generated for a user to use. When the using condition of reusing the micro-nano bubble liquid generating system 100 is satisfied, the circulation control can be performed again according to the above process.
When the liquid level sensor 161 detects that the liquid level height is at the preset liquid level height threshold again, or the water flow sensor 71 detects that the accumulated water flow is greater than the first preset flow L1, or the accumulated service time of the water flow sensor 71 is greater than the first preset time T4, the flow switching valve and the pump body 53 are controlled again to operate, so that the mixing chamber 16 realizes water drainage and air intake during the operation, and the gas in the mixing chamber 16 is supplemented.
When the controller 3 does not detect that the water flow continuous time is greater than T5 by the water flow sensor 71, or the controller 3 determines that the accumulated water flow of the water flow sensor 71 is greater than the second preset flow L2 in the last operation process, or the liquid level detected by the liquid level sensor 161 is higher than the upper limit value of the preset liquid level height threshold, the controller 3 restarts the water outlet switch 61, and controls the mixing chamber 16 to be in the air inlet state, so that a certain amount of air-dissolved liquid is always kept in the mixing chamber 16.
Example 19
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 17, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 23, the liquid outlet end of the liquid separation channel 81 is provided between the pump body 53 and the junction 82. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 17.
Example 20
A micro-nano bubble liquid generating system 100, which has the same structure as that of embodiment 19, wherein the same components are denoted by the same reference numerals, and the differences are only that: as shown in fig. 30, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. The liquid level sensor 161 is communicatively connected to the controller 3, the liquid level sensor 161 is used to detect the liquid level of the liquid in the mixing chamber 16, and the liquid level sensor 161 is disposed at an upper, middle or lower position of the mixing chamber 16. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 18.
Example 21
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 19, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 24, the liquid outlet end of the liquid separation flow path 81 is provided on the liquid outlet flow path 6 and between the liquid outlet 13 and the water outlet switch 61. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 17.
Example 22
A micro-nano bubble liquid generating system 100, having substantially the same structure as that of embodiment 20, wherein the same components are denoted by the same reference numerals, and the difference is that: as shown in fig. 31, the micro-nano bubble liquid generating system 100 further includes a liquid level sensor 161. The liquid level sensor 161 is communicatively connected to the controller 3, the liquid level sensor 161 is used to detect the liquid level of the liquid in the mixing chamber 16, and the liquid level sensor 161 is disposed at an upper, middle or lower position of the mixing chamber 16. The using process of the micro-nano bubble liquid generating system 100 can be seen in example 18.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The principle of micro-nano bubble generation in the micro-nano bubble liquid generating system 100 and the water heater 1000 according to the embodiment of the present invention, and the communication manner between the controller 3 and the components such as the air intake assembly 50, the liquid path pressure regulating valve assembly 70, and the water flow sensor 71 are known to those skilled in the art, and will not be described in detail herein.
In the description herein, references to the description of the terms "embodiment," "example," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
While embodiments of the invention have been shown and described, it will be understood by those of ordinary skill in the art that: various changes, modifications, substitutions and alterations can be made to the embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the claims and their equivalents.
Claims (18)
1. A micro-nano bubble liquid generation system, comprising:
the air dissolving device is internally provided with a mixing cavity and is provided with a liquid inlet flow path and an air inlet path which are communicated with the mixing cavity;
the gas inlet assembly is connected with the gas dissolving device, the gas inlet assembly enables the gas inlet gas path to inlet gas towards the mixing cavity, and gas and liquid in the gas dissolving device are mixed to form gas-liquid mixed liquid; the air inlet assembly comprises a one-way valve, and the one-way valve is arranged on the air inlet path to control the air inlet direction of the air inlet path.
2. The micro-nano bubble liquid generating system according to claim 1, further comprising a liquid path pressure regulating valve assembly, wherein the liquid path pressure regulating valve assembly is disposed on the liquid inlet path, and the liquid path pressure regulating valve assembly is configured to regulate a pressure of the liquid inlet path.
3. The micro-nano bubble liquid generating system according to claim 2, wherein the air inlet assembly includes a pump body, the air dissolving device is formed with a liquid outlet flow path communicated with the mixing chamber, and the pump body is disposed on the liquid outlet flow path and used for pumping liquid in the air dissolving device, so that when the pressure of gas in the air dissolving device is lower than the pressure of gas in the air inlet path, the air inlet path introduces air into the mixing chamber.
4. The micro-nano bubble liquid generating system according to claim 3, wherein the air dissolving device is further provided with a converging flow path communicated with the mixing chamber, one end of the converging flow path is respectively communicated with the liquid inlet flow path and the air inlet path, the other end of the converging flow path is communicated with the mixing chamber, and the pump body is arranged on the converging flow path.
5. The micro-nano bubble liquid generating system according to any one of claims 1 to 4, wherein the air intake assembly comprises an inflator pump, the inflator pump is disposed on the air intake path, and the inflator pump can inflate the mixing chamber.
6. The micro-nano bubble liquid generating system according to any one of claims 2 to 4, further comprising a pressure stabilizing valve, wherein the pressure stabilizing valve is connected in parallel with the liquid path pressure regulating valve assembly.
7. The micro-nano bubble liquid generating system according to claim 6, wherein two ends of the pressure stabilizing valve are connected with the liquid path pressure regulating valve assembly in parallel and then are arranged on the liquid inlet path; or one end of a liquid separating flow path connected with the pressure stabilizing valve is connected to the liquid inlet end of the liquid path pressure regulating valve assembly, and the other end of the liquid separating flow path is connected to the liquid inlet end of the gas dissolving device; or one end of a liquid separating flow path connected with the pressure stabilizing valve is connected to the liquid inlet end of the liquid path pressure regulating valve component, and the other end of the liquid separating flow path is connected to the liquid outlet flow path of the mixing cavity.
8. The micro-nano bubble liquid generating system according to claim 6, wherein the liquid path pressure regulating valve assembly comprises a flow regulating valve, and the pressure stabilizing valve and the flow regulating valve are integrally arranged on the liquid inlet path.
9. The micro-nano bubble liquid generating system according to claim 5, wherein the liquid inlet flow path is communicated with the mixing chamber through a liquid inlet, and the air inlet path is communicated with the mixing chamber through an air inlet; the liquid path pressure regulating valve assembly comprises a water inlet valve and a pressure stabilizing valve, the liquid inlet flow path is provided with the water inlet valve for controlling the on-off of water flow in the liquid inlet flow path and the pressure stabilizing valve for stabilizing the water inlet pressure of the liquid inlet, and the air pressure pumped by the inflator pump is not less than the water inlet pressure of the liquid inlet; or the liquid path pressure regulating valve assembly comprises: and the pressure regulating valve is connected in series on the liquid inlet pipeline, and the water outlet pressure of the pressure regulating valve is adjustable between an upper threshold and a lower threshold.
10. The micro-nano bubble liquid generating system according to claim 9, wherein the inlet valve and the pressure stabilizing valve are connected in series on the inlet flow path in sequence; or the two ends of the water inlet valve are connected with the pressure stabilizing valve in parallel and then are connected with the liquid inlet flow path in series.
11. The micro-nano bubble liquid generating system according to claim 9, wherein the water inlet valve is a two-position three-way valve having two water outlet paths connected in parallel, and the pressure stabilizing valve is connected in series to one of the two water outlet paths.
12. The micro-nano bubble liquid generating system according to claim 9, wherein the pressure stabilizing valve is an adjustable pressure stabilizing valve, and the air pressure pumped by the inflator is not less than a lower threshold of an adjustable pressure range of the adjustable pressure stabilizing valve.
13. The micro-nano bubble liquid generating system according to any one of claims 9 to 12, further comprising: the controller is in communication connection with the inflator pump and is used for controlling the inflator pump to start and stop; or the controller is connected with the pump body of the air inlet assembly and used for controlling the pump body to start and stop.
14. The micro-nano bubble liquid generating system according to claim 13, further comprising: the water flow sensor is arranged on the liquid inlet flow path to detect the liquid inlet flow of the liquid inlet flow path;
the water flow sensor is in communication connection with the controller; the controller is configured to control activation of the inflator or pump body when the water flow sensor detects a water flow signal.
15. The micro-nano bubble liquid generating system according to claim 14, wherein the controller is further in communication connection with the liquid path pressure regulating valve assembly and the air intake assembly, respectively, and is configured to control the liquid path pressure regulating valve assembly to switch from a high water pressure state to a low water pressure state when accumulated water flow of the water flow sensor is greater than a first preset flow or accumulated service time of the water flow sensor is greater than a first preset time, and the controller controls the air intake assembly to operate so as to enter the air intake state.
16. The micro-nano bubble liquid generating system according to claim 15, wherein the controller controls a pump body of the air intake assembly and/or controls an inflator of the air intake assembly to start when the liquid path pressure regulating valve assembly is switched to a low water pressure state.
17. The micro-nano bubble liquid generating system according to claim 1, further comprising a micro-nano bubble generator and a water outlet member, wherein the micro-nano bubble generator is connected with a liquid outlet flow path of the air dissolving device; the water outlet piece is connected to the tail end of the liquid outlet flow path, and the micro-nano bubble generator is arranged in the water outlet piece; the water outlet piece is a shower head or a faucet.
18. A water heater, comprising:
a heating device;
the micro-nano bubble liquid generating system according to any one of claims 1 to 17, wherein an air dissolving device of the micro-nano bubble liquid generating system is arranged at a water outlet end or a water inlet end of the heating device.
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| CN202111673907.0A Pending CN114832661A (en) | 2021-02-01 | 2021-12-31 | Micro-nano bubble liquid generation system and water heater |
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| CN202123456383.8U Active CN217646211U (en) | 2021-02-01 | 2021-12-31 | Integrated adjustable flow valve, micro-nano bubble liquid generation system and water heater |
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| CN217646209U (en) | 2022-10-25 |
| CN217527059U (en) | 2022-10-04 |
| CN114832659A (en) | 2022-08-02 |
| CN114832660A (en) | 2022-08-02 |
| CN217527057U (en) | 2022-10-04 |
| CN114832664A (en) | 2022-08-02 |
| CN114832662A (en) | 2022-08-02 |
| CN217646208U (en) | 2022-10-25 |
| CN216878801U (en) | 2022-07-05 |
| CN216878799U (en) | 2022-07-05 |
| CN114832661A (en) | 2022-08-02 |
| CN217646211U (en) | 2022-10-25 |
| CN217016138U (en) | 2022-07-22 |
| CN114832658A (en) | 2022-08-02 |
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