Micro-nano bubble continuous generation control method, system and device

Abstract

The invention relates to the technical field of nanobubble generation, in particular to a micro-nanobubble continuous generation control method, system and device. The problems that a gas-liquid mixing pump is high in cost, needs an air pump, is large in noise and is limited in application are solved. The device comprises a water pump, a water inlet valve, a vent valve, a water outlet valve, a first pressure dissolved air tank, a second pressure dissolved air tank and an nth pressure dissolved air tank, the water pump is respectively connected with the first pressure air dissolving tank, the second pressure air dissolving tank to the nth pressure air dissolving tank through a plurality of water inlet valves; the top of each pressure dissolved air tank is communicated to the vent valve, and the bottom is communicated to the water outlet valve. The method comprises the following steps: acquiring the number and residual volume of dissolved air tanks, and starting a dissolved air tank switching program and a water production program to form micro-nano bubble water; collecting the generated micro-nano bubble water, and carrying out sampling detection on the micro-nano bubble water; continuous and stable production is achieved, the production efficiency is improved, continuous supply of bubble water is ensured, additional air pump equipment is not needed, and energy conservation and emission reduction are facilitated.

Description

Technical Field

[0001] The present invention relates to the technical field of nano bubble generation, and in particular to a method, system and device for controlling the continuous generation of micro-nano bubbles. Background Art

[0002] Nanobubbles are tiny gaseous bubbles with a diameter usually below 100 nanometers. They have unique physical and chemical properties. They can be formed at the interface between liquid and solid, or suspended in liquid. The formation mechanism of nanobubbles is complex and involves many factors, such as surface tension, adsorption and desorption of gas molecules, and liquid-gas-solid interaction at the interface. There are various methods for generating nanobubbles. The pressurized dissolution release method is the most common method for generating micro-nano bubbles. It uses a pump to mix liquid and gas under a certain pressure, so that the gas dissolves in the liquid to form a supersaturated solution (compared with the saturated solubility at atmospheric pressure). When the supersaturated solution is released to atmospheric pressure, micro-nano bubbles can be generated.

[0003] Prior art 1, Chinese patent, application number: 201310737193.4 discloses a method for generating ozone microbubbles, including controlling the volume ratio of gas to liquid input into the gas-liquid mixing pump to be 1:60-1:40, inputting ozone gas and raw water to be treated into the gas-liquid mixing pump respectively and fully mixing them into dissolved gas water; transporting the dissolved gas water from the gas-liquid mixing pump to a pressure dissolved gas tank; maintaining the pressure in the pressure dissolved gas tank at 0.25MPa-0.4MPa, and outputting dissolved gas water from the pressure dissolved gas tank. Although the utilization rate of ozone and the sewage treatment effect are improved, and the equipment cost and operation difficulty are reduced; however, the cost of the gas-liquid mixing pump is very high and its application is limited.

[0004] Prior art 2, Chinese patent, application number 201511035038.3 discloses a flotation pressure dissolved gas device, including a dissolved gas tank, a micro-nano bubble releaser and a reaction tank, the dissolved gas tank is set as a jet-free filler type, the hydraulic retention time in the dissolved gas tank tube is 5-10 seconds, and the normal working pressure in the tube of the dissolved gas tank is 0.25MPa; the dissolved gas saturation rate of the dissolved gas tank is above 80%, an air inlet is set on the dissolved gas tank, a water inlet is set on the dissolved gas tank, and a water outlet is set on the dissolved gas tank, and the water outlet and the micro-nano bubble releaser are set at the bottom of the reaction tank. Although the flotation pressure dissolved gas device is energy-efficient and easy to manage, by improving the dissolved gas tank and the releaser in the existing dissolved gas device, the volume of the dissolved gas tank is reduced and the bubble generation effect is improved, and the removal rate of impurities is increased; but it requires an air compressor, which is noisy and has limited application.

[0005] Prior art three, Chinese patent, application number 202210778793.4 discloses a control method and processor for a micro-nano bubble liquid generation system, the micro-nano bubble liquid generation system includes a liquid inlet flow channel, a liquid outlet flow channel, an air inlet channel, a gas-liquid mixing chamber and a micro-nano bubble liquid generating device, and the control method includes: determining that the liquid outlet flow channel is in a conducting state; determining that liquid flows in the liquid inlet flow channel for the first time; controlling the closing of the liquid inlet flow channel; conducting the air inlet channel to feed air into the gas-liquid mixing chamber; determining that the air intake time reaches the preset air intake time; stopping the air intake into the gas-liquid mixing chamber, conducting the liquid inlet flow channel to feed liquid into the gas-liquid mixing chamber, so that the dissolved gas liquid in the gas-liquid mixing chamber flows out and releases pressure through the micro-nano bubble liquid generating device to form micro-nano bubble liquid. Although the generated micro-nano bubbles have high density and low cost, they are suitable for application in miniaturized equipment; however, a large number of automatic control valves are required, and the application is limited.

[0006] At present, the prior art 1, prior art 2 and prior art 3 have the problems of high cost of gas-liquid mixing pump, need of air pump, high noise, need of a large number of automatic control valves, and limited application. Therefore, the present invention provides a micro-nano bubble continuous generation control system and device, which uses simple system optimization, does not use gas-liquid mixing pump, air pump, and a large number of automatic control valves, and automatically inhales air to achieve continuous generation of micro-nano bubbles. Summary of the invention

[0007] In order to achieve the above object, the present invention adopts the following technical scheme:

[0008] In one aspect of the present invention, a method for controlling the continuous generation of micro-nano bubbles is provided, the method comprising:

[0009] Obtain the number and remaining volume of several dissolved gas tanks, set the start times of dissolved gas tank switching program according to the number, and obtain the remaining volume of dissolved gas tanks by liquid level sensor;

[0010] When the remaining volume is equal to the total volume of the current dissolved air tank, the current dissolved air tank forms supersaturated water; the dissolved air tank switching program is started, water is pumped into the new dissolved air tank, and the water inlet of the current dissolved air tank is closed; after the dissolved air tank switching program is completed, the water making program of the current dissolved air tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water;

[0011] The generated micro-nano bubble water is collected and sampled for testing, and parameters such as particle size distribution and concentration are tested to optimize the bubble generating device.

[0012] In an optional implementation manner, the process of the liquid level sensor obtaining the remaining volume of the dissolved gas tank includes:

[0013] The number of pressure dissolved gas tanks is determined according to the number of liquid level sensors installed inside each pressure dissolved gas tank, and each pressure dissolved gas tank is numbered, and water is produced in the order of the numbers when producing water;

[0014] According to the number of pressure dissolved gas tanks obtained and the required amount of micro-nano bubble water, and based on the evaluation of the working cycle and capacity of the pressure dissolved gas tanks, the number of startup times of the pressure dissolved gas tank switching program is set;

[0015] The volume of the liquid contained in each pressure dissolved gas tank, ie, the residual volume, is obtained through the liquid level sensor inside each pressure dissolved gas tank.

[0016] In an optional embodiment, the process of switching the dissolved gas tank program includes:

[0017] The remaining volume obtained is compared with the total volume of the current dissolved gas tank. If the remaining volume is less than the total volume of the current dissolved gas tank, the remaining volume data is continued to be obtained; if the remaining volume is equal to the total volume of the current dissolved gas tank, the dissolved gas tank switching program is started;

[0018] Close the water inlet of the current dissolved air tank and open the water inlet of the next dissolved air tank, so that the water in the water pump flows into the next dissolved air tank. After completion, the current dissolved air tank switching program ends;

[0019] After the switching program of the dissolved air tank is completed, the water making program of the current dissolved air tank is started, and the ventilation and water outlet functions of the current dissolved air tank are turned on to form micro-nano bubble water; when the remaining volume is higher than a certain set threshold, the ventilation and water outlet functions of the current dissolved air tank are turned off, and the water making program of the current dissolved air tank is completed.

[0020] In an optional embodiment, the threshold setting process for starting the gas dissolving tank switching program includes:

[0021] Obtain the total designed volume of the dissolved air tank, record the time required for the dissolved air tank to be full from the beginning of filling with water, and record the time required for the dissolved air tank to be completely emptied from the beginning of draining water; calculate the average working time of the dissolved air tank; determine the filling and draining rates of the dissolved air tank under normal working conditions, and set a safety margin, which is set at 5% to 10% of the total volume; the triggering filling threshold or draining threshold is the threshold at which the dissolved air tank needs to trigger filling or draining when a certain liquid level is reached, and the threshold is calculated by subtracting the safety margin from the total volume.

[0022] In an optional embodiment, the process of opening the water inlet of the next dissolved gas tank includes:

[0023] Obtain the total opening value between the valve being fully opened and fully closed, the water inlet valve opening value of the current dissolved air tank, and the water inlet valve opening value of the next dissolved air tank;

[0024] By adjusting the water inlet valves of the current dissolved gas tank and the next dissolved gas tank, the opening of the water inlet valve of the current dissolved gas tank is equal to the difference between the total opening value and the opening value of the next dissolved gas tank;

[0025] Monitor the water pressure of the water flowing out of the water pump in real time. When the current water pressure value is monitored to be lower than the preset water pressure threshold, continue monitoring. When the current water pressure value is monitored to be higher than the preset water pressure threshold, slow down the closing speed of the current dissolved air tank water inlet valve and speed up the opening speed of the next dissolved air tank water inlet valve until the water pressure is below the preset water pressure threshold.

[0026] In an optional implementation, the process of starting the ventilation and water outlet functions of the current dissolved gas tank includes:

[0027] Start the water production program, slowly open the ventilation valve of the current dissolved air tank, a one-way valve should be set between the ventilation valve and the dissolved air tank, and collect the opening value of the ventilation valve of the current dissolved air tank in real time;

[0028] Slowly open the water outlet valve of the current dissolved air tank, and collect the opening value of the water outlet valve of the current dissolved air tank in real time;

[0029] The flow rate of the micro-nano bubble water outside the water outlet valve is collected in real time, and the collected flow rate data is compared with the preset flow rate interval value. If the collected flow rate value is lower than the interval value, the ventilation valve and the water outlet valve of the current dissolved gas tank will continue to be opened; if the collected flow rate value is within the interval, the current opening of the two valves will be maintained; if the collected flow rate value is higher than the interval value, the opening of the two valves will be slowly reduced until the flow rate value is within the flow rate interval.

[0030] In an optional embodiment, the process of sampling and detecting micro-nano bubble water includes:

[0031] After the dissolved air tank completes the water production process, the micro-nano bubble water flowing out of the water outlet valve is sampled to detect the particle size and concentration of micron bubbles and nano bubbles respectively;

[0032] The produced micro-nano bubble water is sampled again and placed in a sample pool to generate its particle size distribution curve and provide statistical information such as its average value and median particle size; image processing and analysis are performed on the remaining sampled micro-nano bubble water to calculate its bubble volume fraction and concentration;

[0033] If the obtained particle size data or bubble concentration data is lower than the qualified threshold of micro-nano bubble water, the number and unqualified information of the current dissolved air tank will be displayed through the visualization device, and the staff will be reminded to deal with it in time through the alarm.

[0034] In an optional implementation, the process of calculating the volume fraction and concentration of the bubbles includes:

[0035] Convert the color image into a grayscale image, use the Canny edge detection algorithm to identify the edges of microbubbles, and identify the connected areas in the image, each of which represents a bubble;

[0036] The volume of the microbubbles is calculated by the diameter of the detected microbubbles, and the volumes of all detected microbubbles are added together to obtain the total bubble volume;

[0037] The total number of detected microbubbles is counted, the calculated volume fraction and concentration are recorded in a database, and the calculated results are compared with a preset qualified threshold value; nanobubbles can be detected using an online laser particle size analyzer DLS, etc.

[0038] Another aspect of the present invention provides a micro-nano bubble continuous generation control system, which implements the micro-nano bubble continuous generation control method. The micro-nano bubble continuous generation control system comprises:

[0039] The data acquisition module is responsible for obtaining the number and remaining volume of several dissolved gas tanks, setting the start times of the dissolved gas tank switching program according to the number, and obtaining the remaining volume of the dissolved gas tank by the liquid level sensor;

[0040] The air dissolving tank switching module, when the remaining volume is equal to the total volume of the current air dissolving tank, the current air dissolving tank forms supersaturated water; the air dissolving tank switching program is started, water is pumped into the new air dissolving tank, and the water inlet of the current air dissolving tank is closed; after the air dissolving tank switching program is completed, the water making program of the current air dissolving tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water;

[0041] The quality detection module collects the generated micro-nano bubble water and performs sampling inspection on it, sampling and inspecting its parameters such as particle size distribution and concentration, so as to optimize the bubble generating device.

[0042] Another aspect of the present invention provides a micro-nano bubble continuous generation control device, which implements the micro-nano bubble continuous generation control method, and the micro-nano bubble continuous generation control device comprises: a water pump, a water inlet valve, a vent valve, a water outlet valve, a first pressure dissolved gas tank, a second pressure dissolved gas tank, and an nth pressure dissolved gas tank;

[0043] The water pump is connected to the first pressure dissolved gas tank, the second pressure dissolved gas tank and the nth pressure dissolved gas tank through multiple water inlet valves; the top of each pressure dissolved gas tank is connected to the vent valve, and the bottom of each pressure dissolved gas tank is connected to the water outlet valve or the water collection tank.

[0044] The present invention can form supersaturated water by introducing water flow from a water pump into multiple pressure gas dissolving tanks and dissolving gas in the tanks. When the supersaturated water is released through a water outlet valve, a large number of micro-nano bubbles are naturally generated, and no additional air pump equipment is required, thereby reducing energy consumption and costs. The device is designed with multiple pressure gas dissolving tanks, which can sequentially carry out the process of dissolving gas and releasing bubbles. When the gas in one tank is completely dissolved and the bubbles are released, it can be quickly switched to the next tank to achieve continuous and stable production, improve production efficiency, and ensure the continuous supply of bubble water. By controlling the switches of the water inlet valve, the vent valve and the water outlet valve, the automatic operation of the device can be achieved, the operation process is simplified, and the safety and stability of production are improved. No additional air pump equipment is required, the energy consumption during operation is low, and it is beneficial to energy saving and emission reduction. BRIEF DESCRIPTION OF THE DRAWINGS

[0045] The accompanying drawings are used to provide a further understanding of the present invention and constitute a part of the specification. Together with the embodiments of the present invention, they are used to explain the present invention and do not constitute a limitation of the present invention. In the accompanying drawings:

[0046] Figure 1 This is a flow chart of the steps of the method for controlling the continuous generation of micro-nano bubbles provided in Example 1 of the present invention;

[0047] Figure 2 A flow chart of the steps of obtaining the remaining volume of the dissolved gas tank by the liquid level sensor provided in Example 2 of the present invention;

[0048] Figure 3 A flow chart of the steps of the gas dissolving tank switching procedure provided in Example 3 of the present invention;

[0049] Figure 4 A flow chart of the steps of opening the water inlet of the next gas dissolving tank provided in Example 4 of the present invention;

[0050] Figure 5 A flow chart of the steps of ventilating and discharging water from the aeration tank provided in Example 5 of the present invention;

[0051] Figure 6 This is a flow chart of the steps of detecting micro-nano bubble water provided in Example 6 of the present invention;

[0052] Figure 7 This is a block diagram of a micro-nano bubble continuous generation control system provided in Example 7 of the present invention;

[0053] Figure 8 This is a schematic structural diagram of a micro-nano bubble continuous generation control device provided in Example 8 of the present invention;

[0054] Fig. 9 A block diagram of an electronic device provided by the present invention;

[0055] Fig.10 A block diagram of a computer-readable storage medium provided for the present invention. DETAILED DESCRIPTION

[0056] The technical solutions in the embodiments of the present invention will be described below in conjunction with the drawings in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, rather than all the embodiments.

[0057] In the following, the terms "first", "second", etc. are used only for convenience of description and should not be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Thus, a feature defined as "first", "second", etc. may explicitly or implicitly include one or more of the features. In the description of the present invention, unless otherwise specified, "plurality" means two or more.

[0058] In the present invention, unless otherwise clearly specified and limited, the term "connection" should be understood in a broad sense, for example, "connection" can be a fixed mechanical connection, or a detachable mechanical connection, or integrated; or, "connection" can be a direct connection, or an indirect connection through an intermediate medium. In addition, unless otherwise clearly specified and limited, the term "coupling" should be understood in a broad sense, for example, "coupling" can be a direct electrical connection, such as physical contact and electrical conduction between two components, and can also be understood as electrical connection between different components in a circuit structure through physical lines such as copper foil or wires on a printed circuit board (PCB) that can transmit electrical signals to transmit electrical signals; or, "coupling" can be an indirect electrical connection between two components through an intermediate medium; or, "coupling" can be an electrical connection between two components in an air-spaced / non-contact manner, for example, two components are electrically connected by capacitive coupling to transmit electrical signals.

[0059] In the embodiments of the present invention, directional terms such as "up", "down", "left" and "right" may be defined including but not limited to the orientation relative to the schematic placement of the components in the drawings. It should be understood that these directional terms may be relative concepts, which are used for relative description and clarification, and may change accordingly according to the change of the orientation of the components in the drawings.

[0060] The embodiments of the present invention can be widely used in multiple fields, including but not limited to: water treatment industry: used to improve water quality and remove harmful substances in water; agricultural irrigation: using micro-nano bubble water to improve soil permeability and fertility; food processing: used for food cleaning and preservation to improve food safety; medical care: used for skin care and wound healing to promote cell regeneration; through this precise control method, the generation process of micro-nano bubbles is more stable and efficient, which can meet the needs of different industries for high-quality micro-nano bubble water.

[0061] Embodiment 1:

[0062] like Figure 1 As shown, the micro-nano bubble continuous generation control method provided by the embodiment of the present invention comprises the following steps:

[0063] Step S100: obtaining the number and remaining volume of a plurality of dissolved gas tanks, setting the start times of the dissolved gas tank switching program according to the number, and obtaining the remaining volume of the dissolved gas tank by the liquid level sensor;

[0064] Step S200: when the remaining volume is equal to the total volume of the current air dissolving tank, the current air dissolving tank forms supersaturated water; the air dissolving tank switching program is started, water is pumped into the new air dissolving tank, and the water inlet of the current air dissolving tank is closed; after the air dissolving tank switching program is completed, the water making program of the current air dissolving tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water;

[0065] Step S300: Collect the generated micro-nano bubble water and perform sampling tests on it, sampling and testing parameters such as particle size distribution and concentration, so as to optimize the bubble generating device.

[0066] In the above embodiment, step S100 of this embodiment accurately obtains the number and remaining volume of the dissolved gas tank, sets the number of startup times of the program according to the number of dissolved gas tanks, and ensures the orderly conduct of the switching operation; the liquid level sensor monitors the remaining volume of the dissolved gas tank in real time to improve the accuracy and real-time performance of the data; step S200, when the remaining volume is equal to the total volume, determines that the current dissolved gas tank has been measured to be supersaturated with water, and starts the switching program in time; after the switching program is completed, starts the water making program to realize the continuous water making of the dissolved gas tank; turns on the ventilation and release functions to form micro-nano bubble water to meet the production needs; step S300 collects the generated micro-nano bubble water, and performs sampling and testing to ensure its quality; the sampled samples are tested for parameters such as particle size distribution and concentration to generate bubbles It provides a basis for the optimization of the device; optimizes the device according to the test results to improve the quality and efficiency of bubble generation; provides reliable data support for the stable operation of the device, avoiding operational errors caused by inaccurate data; improves the degree of automation of the device and reduces the need for manual intervention; ensures continuous water production and stable generation of bubble water in the dissolved air tank, and improves production efficiency; avoids safety hazards caused by oversaturation of the dissolved air tank by timely switching of the dissolved air tank; ensures the quality of micro-nano bubble water and meets the needs of different application scenarios; improves the performance and stability of the bubble generating device through continuous quality testing and device optimization; provides reliable technical support and guarantee for the application of micro-nano bubble technology, and promotes the development of related industries.

[0067] Embodiment 2:

[0068] like Figure 2 As shown, based on Example 1, the process of obtaining the remaining volume of the dissolved gas tank by the liquid level sensor in step S100 provided in the embodiment of the present invention includes the following steps:

[0069] Step S101: determining the number of pressure-dissolving gas tanks according to the number of liquid level sensors installed inside each pressure-dissolving gas tank, and numbering each pressure-dissolving gas tank, and producing water in the order of the numbers when producing water;

[0070] Step S102: according to the acquired number of pressure dissolved gas tanks and the required amount of micro-nano bubble water, and according to the evaluation of the working cycle and capacity of the pressure dissolved gas tanks, the number of startup times of the pressure dissolved gas tank switching program is set;

[0071] Among them, the equation for calculating the switching times of the pressure gas tank is:

[0072]

[0073] Where N switch Indicates the number of times the pressure gas tank switching program is started, Q total Indicates the total amount of water with micro-nano bubbles required, in cubic meters (m3 ), T cycle It indicates the working cycle of the pressure gas tank in hours (h), ΔT indicates the change of ambient temperature in degrees Celsius (℃), T ref represents the reference temperature in degrees Celsius (°C), ΔP represents the pressure change in Pascal (Pa), P ref Indicates the reference pressure in Pascal (Pa), V tank Indicates the capacity of a single pressure gas tank in cubic meters (m 3 ), η represents the efficiency coefficient of the pressure gas tank, which represents the utilization rate of the gas tank in actual work, usually a value between 0 and 1, L initial Indicates the initial liquid level of the dissolved gas tank in cubic meters (m 3 ), σ sensor Indicates the accuracy of the liquid level sensor in cubic meters (m 3 ), L max Indicates the maximum measuring range of the liquid level sensor in cubic meters (m 3 ), Indicates the rounding symbol, indicating that the calculation result is rounded up to the nearest integer; the temperature and pressure correction factors are and It is used to correct the influence of ambient temperature and pressure changes on the operation of the dissolved gas tank. The initial liquid level correction factor is expressed as It is used to consider the effect of the initial liquid level of the dissolved gas tank on the available volume. The sensor accuracy correction factor is expressed as Used to consider the influence of the accuracy of the liquid level sensor on the measurement results. Through this equation, the number of switching times of the pressure gas tank can be calculated more accurately, ensuring efficient water production operation under various practical conditions;

[0074] Step S103: obtaining the volume of the liquid contained in each pressure dissolved gas tank, ie, the residual volume, through the liquid level sensor inside each pressure dissolved gas tank.

[0075] In the above embodiment, step S101 determines the number of pressure gas tanks according to the number of liquid level sensors, and numbers each tube, and water production is carried out in the order of numbers; it is ensured that each pressure gas tank is effectively utilized and the water production process is carried out in an orderly manner; by making water by numbering and sequence, the water production efficiency can be improved, confusion and errors can be reduced, and the load balance of each tank can be ensured; step S102 sets the number of startup times of the switching program according to the number of pressure gas tanks, the required amount of micro-nano bubble water, and the evaluation of the working cycle and capacity; it is ensured that the water supply in the water production process matches the demand to avoid waste or shortage of resources; by reasonably setting the number of switching times, the water production process can be optimized, the resource utilization rate can be improved, and the demand for micro-nano bubble water can be met; step S103 obtains the remaining volume in each pressure gas tank through the liquid level sensor; the liquid volume in the tank is monitored in real time to provide a basis for switching and water production decisions; through real-time monitoring, the water production strategy and switching sequence can be adjusted in time to avoid too much or too little liquid in the tank, and ensure the stability and efficiency of the water production process.

[0076] Embodiment 3:

[0077] like Figure 3 As shown, based on Example 1, the process of switching the gas tank in step S200 provided in the embodiment of the present invention includes the following steps:

[0078] Step S201: Compare the obtained remaining volume with the total volume of the current dissolved gas tank. If the remaining volume is less than the total volume of the current dissolved gas tank, continue to obtain the remaining volume data; if the remaining volume is equal to the total volume of the current dissolved gas tank, start the dissolved gas tank switching program;

[0079] Among them, the threshold setting process for starting the dissolved gas tank switching program:

[0080] Obtain the total designed volume of the dissolved air tank, record the time required for the dissolved air tank to be full from the beginning of filling with water, and record the time required for the dissolved air tank to be completely emptied from the beginning of draining water; calculate the average working time of the dissolved air tank; determine the filling and draining rates of the dissolved air tank under normal working conditions, and set a safety margin, which is set at 5% to 10% of the total volume; the triggering filling threshold or draining threshold is the threshold at which the dissolved air tank needs to trigger filling or draining when a certain liquid level is reached, and the threshold is calculated by subtracting the safety margin from the total volume.

[0081] Step S202: close the water inlet of the current dissolved gas tank, and open the water inlet of the next dissolved gas tank, so that the water in the water pump flows into the next dissolved gas tank, and the current dissolved gas tank switching program ends after completion;

[0082] Step S203: After the gas tank switching program is completed, the water production program of the current gas tank is started, and the ventilation and water outlet functions of the current gas tank are turned on to form micro-nano bubble water; when the remaining volume is higher than a certain set threshold, the ventilation and water outlet functions of the current gas tank are turned off, and the water production program of the current gas tank is completed.

[0083] In the above embodiment, step S201 of this embodiment detects the remaining volume of the dissolved gas tank in real time to ensure the accuracy and timeliness of the data; by comparing the remaining volume and the total volume, it is determined whether the dissolved gas tank switching program needs to be started; the situation of overfilling or premature switching of the dissolved gas tank is avoided, and the operation efficiency and stability of the equipment are improved; the continuity of the water production process is ensured, and it will not be interrupted due to the switching of the dissolved gas tank; step S202 realizes the smooth switching of the dissolved gas tank, avoiding the influence of sudden interruption or change of water flow on the system; by closing and opening the water inlet valve, it is ensured that the water in the water pump can smoothly flow into the lower a dissolved air tank; ensures the continuity of the water production process, while avoiding equipment damage or safety accidents caused by improper switching; improves the degree of automation of the equipment, and reduces the complexity and error of manual operation; after starting the water production program in step S203, the dissolved air tank begins to produce micro-nano bubble water, meeting specific water production needs; when the remaining volume is higher than a certain set threshold, the ventilation and water outlet functions are closed in time, ensuring the efficiency and accuracy of the water production process, and meeting the user's demand for micro-nano bubble water; by precisely controlling the ventilation and water outlet functions, the rational use and conservation of energy is achieved.

[0084] Embodiment 4:

[0085] like Figure 4 As shown, based on Example 3, the process of opening the water inlet of the next dissolved gas tank in step S202 provided in the embodiment of the present invention includes the following steps:

[0086] Step S2021: obtaining the total opening value between the valve being fully opened and fully closed, the opening value of the water inlet valve of the current dissolved gas tank, and the opening value of the water inlet valve of the next dissolved gas tank;

[0087] Step S2022: adjusting the water inlet valves of the current gas dissolving tank and the next gas dissolving tank so that the opening of the water inlet valve of the current gas dissolving tank is equal to the difference between the total opening value and the opening value of the next gas dissolving tank;

[0088] Step S2023: monitor the water pressure of the water flowing out of the water pump in real time. When the current water pressure value is monitored to be less than the preset water pressure threshold, continue monitoring; when the current water pressure value is monitored to be higher than the preset water pressure threshold, slow down the closing speed of the current dissolved air tank water inlet valve and speed up the opening speed of the next dissolved air tank water inlet valve until the water pressure is below the preset water pressure threshold.

[0089] In the above embodiment, step S2021 of this embodiment first obtains the total valve opening value, the water inlet valve opening value of the current dissolved gas tank and the water inlet valve opening value of the next dissolved gas tank. By obtaining these key data, it can be ensured that the adjustment process is based on accurate information, which helps to achieve more accurate flow distribution and pressure control; step S2022 adjusts the water inlet valves of the current dissolved gas tank and the next dissolved gas tank according to the obtained data, so that the opening of the water inlet valve of the current dissolved gas tank is equal to the difference between the total opening value and the opening value of the next dissolved gas tank, thereby achieving reasonable distribution of flow; by accurately adjusting the opening of the water inlet valve, it can be ensured that Ensure the stable operation of the system and avoid efficiency loss or equipment damage caused by uneven flow distribution; step S2023 monitors the water pressure flowing out of the water pump in real time, and adjusts the opening and closing speed of the water inlet valve according to the water pressure value. When the water pressure is about to reach the preset threshold, the water pressure is adjusted by slowing down the closing speed of the current dissolved air tank water inlet valve and accelerating (the involved slowing down and accelerating are preset by the system) the opening speed of the next dissolved air tank water inlet valve; ensure that the water pressure of the system is always within a safe and stable range; by dynamically adjusting the opening and closing speed of the water inlet valve, problems such as equipment damage or system instability caused by excessive water pressure can be effectively avoided.

[0090] Embodiment 5:

[0091] like Figure 5 As shown, based on Example 3, the process of starting the ventilation and water outlet functions of the current dissolved gas tank in step S203 provided in the embodiment of the present invention includes the following steps:

[0092] Step S2031: Start the water production program, slowly open the ventilation valve of the current dissolved gas tank, a one-way valve should be set between the ventilation valve and the dissolved gas tank, and collect the opening value of the ventilation valve of the current dissolved gas tank in real time;

[0093] Step S2032: slowly opening the water outlet valve of the current dissolved gas tank, and collecting the opening value of the water outlet valve of the current dissolved gas tank in real time;

[0094] Step S2033: collect the flow rate of the micro-nano bubble water outside the water outlet valve in real time, and compare the collected flow rate data with the preset flow rate interval value. If the collected flow rate value is lower than the interval value, continue to open the ventilation valve and the water outlet valve of the current dissolved gas tank; if the collected flow rate value is within the interval, maintain the current opening of the two valves; if the collected flow rate value is higher than the interval value, slowly reduce the opening of the two valves until the flow rate value is within the flow rate interval.

[0095] In the above embodiment, step S2031 of this embodiment ensures that the entire water production system starts to operate, avoids the impact on the system due to sudden pressure changes during ventilation, and ensures the stable operation of the system; ensures the smooth start of the water production process to avoid damage due to sudden pressure changes in the system; step S2032 protects the micro-nano bubble water from sudden pressure changes and provides a data basis for the precise control of the system; step S2033 provides real-time information on the water outlet status of the system to ensure that the water outlet flow rate meets the design requirements and is neither too fast nor too slow; when the flow rate is lower than the interval value, the valve continues to be opened to increase the flow rate to ensure the water outlet efficiency; when the flow rate is within the interval, the current state is maintained to ensure the stable operation of the system; when the flow rate is higher than the interval value, the valve opening is reduced to reduce the flow rate to avoid damage to the quality of the micro-nano bubble water.

[0096] Embodiment 6:

[0097] like Figure 6 As shown, based on Example 1, the process of detecting micro-nano bubble water in step S300 provided in the embodiment of the present invention includes the following steps:

[0098] Step S301: After the current dissolved gas tank completes the water production process, the micro-nano bubble water flowing out of the water outlet valve is sampled to detect the particle size and concentration of micron bubbles and nano bubbles respectively;

[0099] Step S302: re-sample the produced micro-nano bubble water and put the sample into a sample pool to generate its particle size distribution curve and provide statistical information such as its average value and median particle size; perform image processing and analysis on the remaining sampled micro-nano bubble water to calculate its bubble volume fraction and concentration;

[0100] The process of calculating the volume fraction and concentration of bubbles includes:

[0101] Convert the color image into a grayscale image, use the Canny edge detection algorithm to identify the edges of microbubbles, and identify the connected areas in the image, each of which represents a microbubble;

[0102] The volume of the microbubbles is calculated by the diameter of the detected microbubbles, and the volumes of all detected microbubbles are added together to obtain the total bubble volume;

[0103] Count the total number of microbubbles detected, record the calculated volume fraction and concentration in a database, and compare the calculated results with the preset qualified threshold;

[0104] Step S303: If the obtained particle size data or bubble concentration data is lower than the qualified threshold of micro-nano bubble water, the number of the current dissolved gas tank and the unqualified information are displayed through the visualization device, and the staff is reminded to deal with it in time through the alarm sound.

[0105] In the above embodiment, in step S301 of this embodiment, after the current dissolved gas tank completes the water production procedure, the micro-nano bubble water flowing out of the water outlet valve is sampled, and the particle size and concentration of micron bubbles and nano bubbles are detected respectively, so as to ensure that representative samples are obtained from the micro-nano bubble water produced by the dissolved gas tank for analysis and evaluation; sampling is the primary step of quality control, which provides basic data for evaluation and ensures the accuracy and reliability of the analysis results; step S302 resamples the produced micro-nano bubble water and analyzes its particle size distribution and bubble concentration; through the particle size distribution curve and statistical information, the bubble concentration can be understood. The size distribution and average size of the bubbles, while the volume fraction and concentration of the bubbles reflect the density of the bubbles; accurate measurement of the particle size and concentration of the bubbles helps to evaluate the quality and performance of the micro-nano bubble water and ensure that the product meets the predetermined standards and requirements; if the data is lower than the qualified threshold in step S303, the staff is reminded through visualization equipment and alarm sound, which realizes real-time monitoring and rapid response. When unqualified products are detected, the staff can be notified immediately for processing; through timely feedback and alarms, unqualified products can be prevented from entering the market, product quality can be guaranteed, and production efficiency and safety can be improved. Nanobubble detection can be carried out by online laser particle size analyzer DLS, etc.

[0106] Embodiment 7:

[0107] like Figure 7 As shown, based on Examples 1 to 6, the micro-nano bubble continuous generation control device system provided by the embodiment of the present invention comprises:

[0108] The data acquisition module is responsible for obtaining the number and remaining volume of several dissolved gas tanks, setting the start times of the dissolved gas tank switching program according to the number, and obtaining the remaining volume of the dissolved gas tank by the liquid level sensor;

[0109] The air dissolving tank switching module, when the remaining volume is equal to the total volume of the current air dissolving tank, the current air dissolving tank forms supersaturated water; the air dissolving tank switching program is started, water is pumped into the new air dissolving tank, and the water inlet of the current air dissolving tank is closed; after the air dissolving tank switching program is completed, the water making program of the current air dissolving tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water;

[0110] The quality detection module collects the generated micro-nano bubble water and performs sampling inspection on it, sampling and inspecting its parameters such as particle size distribution and concentration, so as to optimize the bubble generating device.

[0111] In the above embodiments, the data acquisition module of this embodiment obtains the number and remaining volume information of the dissolved gas tank in real time and accurately; intelligently sets the number of startup times of the switching program according to the number of dissolved gas tanks to ensure the continuity and efficiency of the system operation; uses the liquid level sensor to accurately monitor the remaining volume of the dissolved gas tank to improve the accuracy and real-time performance of data acquisition; provides reliable data support for the intelligent operation of the system to ensure that the system can be dynamically adjusted according to actual needs; improves the automation level of the system, reduces manual intervention, and reduces operating costs; provides accurate basis for the switching of dissolved gas tanks and the startup of water production programs to ensure the stable operation of the system; the dissolved gas tank switching module starts the switching program in time when the dissolved gas tank reaches an oversaturated state to avoid system overload and safety hazards; ensures that water is pumped into the new dissolved gas tank during the switching process, and at the same time closes the water inlet of the current dissolved gas tank to achieve seamless switching; after the switching is completed Automatically start the water making program, and turn on the ventilation and release functions to ensure the stable generation of micro-nano bubble water; improve the reliability and stability of the system to ensure the continuous production of micro-nano bubble water; by timely switching the dissolved gas tank, extend the service life of the dissolved gas tank and reduce maintenance costs; optimize the operating efficiency of the system to improve the output and quality of micro-nano bubble water; the quality inspection module samples and inspects the generated micro-nano bubble water to ensure that it meets the quality standards; by detecting parameters such as the particle size distribution and concentration of the upper layer samples, provide data support for the optimization of the bubble generating device; optimize the device in a targeted manner according to the test results to improve the efficiency and stability of bubble generation; ensure the quality and safety of micro-nano bubbles to meet user needs; improve the performance and stability of the system through continuous quality inspection and device optimization; provide reliable technical support and guarantee for the application of micro-nano bubble technology.

[0112] like Figure 8 As shown, the embodiment of the present invention provides a micro-nano bubble continuous generation control device, comprising: a water pump 1, a water inlet valve 2, a vent valve 3, a water outlet valve 4, a first pressure dissolved gas tank 5, a second pressure dissolved gas tank 6, and an nth pressure dissolved gas tank 7;

[0113] Among them, the water pump 1 is connected to the first pressure dissolved gas tank 5, the second pressure dissolved gas tank 6 and the nth pressure dissolved gas tank 7 through multiple water inlet valves 2; the top of each pressure dissolved gas tank is connected to the vent valve 3, and the bottom of each pressure dissolved gas tank is connected to the water outlet valve 4 or connected to the water collection tank respectively.

[0114] In the above embodiment, the first air dissolving tank 5 of this embodiment is hollow before the water pump 1 is started, that is, there is air inside. When the water pump 1 is started to allow water to enter the first pressure air dissolving tank 5, the gas in the tank will continuously dissolve into the water to form supersaturated water, and micro-nano bubbles will be generated through the water outlet valve 4; the gas in the tank will continuously dissolve into the water, and the liquid level will continuously rise until all the gas in the tank is dissolved. At this time, the water inlet valve 2 of the first air dissolving tank 5 is closed, and the water outlet of the water pump 1 is switched to the second pressure air dissolving tank 6, and the dissolved gas is released repeatedly to generate micro-nano bubbles; at the same time, the vent valve 3 on the top of the first pressure air dissolving tank 5 is opened, and the solution retained in the tube flows out by gravity through the water outlet valve 4, and air enters naturally; in this order, micro-nano bubble water can be continuously generated, but no air pump is required; by introducing the water flow of the water pump into the second pressure air dissolving tank 6, the air outlet valve 3 on the first pressure air dissolving tank 5 is opened, and the solution retained in the tube flows out by gravity through the water outlet valve 4, and air enters naturally. Multiple pressure gas dissolving tanks are stored in the tanks, and gas is dissolved in the tanks to form supersaturated water. When the supersaturated water is released through the water outlet valve, a large number of micro-nano bubbles are naturally generated, and no additional air pump equipment is required, thereby reducing energy consumption and costs. The device is designed with multiple pressure gas dissolving tanks, which can sequentially carry out the process of dissolving gas and releasing bubbles. When the gas in a tank is completely dissolved and the bubbles are released, it can be quickly switched to the next tank to achieve continuous and stable production, improve production efficiency, and ensure a continuous supply of bubble water. By controlling the switches of the water inlet valve, the vent valve and the water outlet valve, the automatic operation of the device can be achieved, the operating process is simplified, and the safety and stability of production are improved. No additional air pump equipment is required, and the energy consumption during operation is low, which is conducive to energy conservation and emission reduction.

[0115] Fig. 9 A block diagram of an exemplary electronic device suitable for implementing embodiments of the present invention is shown.

[0116] The electronic device may include a central processing unit / microprocessor / main control chip, etc.; a storage medium, coupled to the central processing unit / microprocessor / main control chip, etc., and storing computer executable instructions therein, for performing the steps of each method of an embodiment of the present invention when executed by the processor.

[0117] The central processing unit / microprocessor / main control chip etc. may include but are not limited to, for example, one or more processors or microprocessors etc.

[0118] The storage medium may include, but is not limited to, for example, random access memory (RAM), read-only memory (ROM), flash memory, EPROM memory, EEPROM memory, registers, computer storage media (e.g., hard disk, floppy disk, solid-state drive, removable disk, CD-ROM, DVD-ROM, Blu-ray disc, etc.).

[0119] In addition, the electronic device may also include (but not limited to) a data bus, an input / output bus / external bus / device bus, a display, and input / output devices (eg, keyboard, mouse, speaker, etc.), etc.

[0120] The central processing unit / microprocessor / main control chip etc. can communicate with external devices via an I / O bus via a wired or wireless network (not shown).

[0121] The storage medium may also store at least one computer executable instruction for executing the various functions and / or method steps in the embodiments described in the present technology when executed by a central processing unit / microprocessor / main control chip, etc.

[0122] In one embodiment, the at least one computer executable instruction may also be compiled into or constitute a software product, wherein one or more computer executable instructions are executed by a processor to perform the various functions and / or method steps in the embodiments described in the present technology.

[0123] Fig.10 A schematic diagram of a computer-readable storage medium according to an embodiment of the present invention is shown.

[0124] like Fig.10 As shown, instructions are stored on the non-transitory computer-readable storage medium, and the instructions are, for example, computer-readable instructions. When the computer-readable instructions are executed by the processor, the various methods described above can be executed. The non-transitory computer-readable storage medium includes, but is not limited to, for example, volatile memory and / or non-volatile memory. Volatile memory may, for example, include random access memory (RAM) and / or cache memory (cache), etc. The non-transitory non-volatile memory may, for example, include read-only memory (ROM), hard disk, flash memory, etc. For example, the non-transitory computer-readable storage medium can be connected to a computing device such as a computer, and then, when the computing device runs the computer-readable instructions stored on the computer-readable storage medium 920, the various methods described above can be performed.

[0125] In the several embodiments provided by the present invention, it should be understood that the disclosed devices and methods can be implemented in other ways. For example, the device embodiments described above are only schematic, for example, the division of units is only a logical function division, and there may be other division methods in actual implementation, such as multiple units or components can be combined or integrated into another system, or some features can be ignored or not executed. Another point is that the mutual coupling or direct coupling or communication connection shown or discussed can be through some interfaces, indirect coupling or communication connection of devices or units, which can be electrical, mechanical or other forms.

[0126] The units described as separate components may or may not be physically separated, and the components shown as units may or may not be physical units, that is, they may be located in one place or distributed on multiple network units. Some or all of the units may be selected according to actual needs to achieve the purpose of the solution of this embodiment.

[0127] In addition, each functional unit in each embodiment of the present invention may be integrated into one processing unit, or each unit may exist physically separately, or two or more units may be integrated into one unit. The above-mentioned integrated unit may be implemented in the form of hardware or in the form of software functional units.

[0128] If the integrated unit is implemented in the form of a software functional unit and sold or used as an independent product, it can be stored in a computer-readable storage medium. Based on this understanding, the technical solution of the present invention, in essence, or the part that contributes to the prior art, or all or part of the technical solution can be embodied in the form of a software product, and the computer software product is stored in a storage medium, including a number of instructions for executing all or part of the steps of the various embodiments of the method of the present invention through a computer device (which can be a personal computer, a server, or a network device, etc.). The aforementioned storage medium includes: U disk, mobile hard disk, read-only memory (full name in English: Read-Only Memory, English abbreviation: ROM), random access memory (full name in English: Random Access Memory, English abbreviation: RAM), disk or optical disk and other media that can store program codes.

[0129] The above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit the same. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that the technical solutions described in the aforementioned embodiments may still be modified, or some of the technical features thereof may be replaced by equivalents. However, these modifications or replacements do not deviate the essence of the corresponding technical solutions from the spirit and scope of the technical solutions of the embodiments of the present invention.

Claims

1. A method for controlling the continuous generation of micro-nano bubbles, characterized in that: The method for controlling the continuous generation of micro-nano bubbles comprises: Obtain the number and remaining volume of several dissolved gas tanks, set the start times of dissolved gas tank switching program according to the number, and obtain the remaining volume of dissolved gas tanks by liquid level sensor; When the remaining volume is equal to the total volume of the current dissolved air tank, the current dissolved air tank forms supersaturated water; the dissolved air tank switching program is started, water is pumped into the new dissolved air tank, and the water inlet of the current dissolved air tank is closed; after the dissolved air tank switching program is completed, the water making program of the current dissolved air tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water; The generated micro-nano bubble water is collected and sampled for testing, and the particle size distribution and concentration parameters are tested to optimize the bubble generating device.

2. The method for controlling the continuous generation of micro-nano bubbles according to claim 1, characterized in that: The process of the liquid level sensor obtaining the remaining volume of the dissolved gas tank includes: The number of pressure dissolved gas tanks is determined according to the number of liquid level sensors installed inside each pressure dissolved gas tank, and each pressure dissolved gas tank is numbered, and water is produced in the order of the numbers when producing water; According to the number of pressure dissolved gas tanks obtained and the required amount of micro-nano bubble water, and based on the evaluation of the working cycle and capacity of the pressure dissolved gas tanks, the number of startup times of the pressure dissolved gas tank switching program is set; The volume of the liquid contained in each pressure dissolved gas tank, ie, the residual volume, is obtained through the liquid level sensor inside each pressure dissolved gas tank.

3. The method for controlling the continuous generation of micro-nano bubbles according to claim 1, characterized in that: The process of the dissolved gas tank switching procedure includes: The remaining volume obtained is compared with the total volume of the current dissolved gas tank. If the remaining volume is less than the total volume of the current dissolved gas tank, the remaining volume data is continued to be obtained; if the remaining volume is equal to the total volume of the current dissolved gas tank, the dissolved gas tank switching program is started; Close the water inlet of the current dissolved air tank and open the water inlet of the next dissolved air tank, so that the water in the water pump flows into the next dissolved air tank. After completion, the current dissolved air tank switching program ends; After the switching program of the dissolved air tank is completed, the water making program of the current dissolved air tank is started, and the ventilation and water outlet functions of the current dissolved air tank are turned on to form micro-nano bubble water; when the remaining volume is higher than a certain set threshold, the ventilation and water outlet functions of the current dissolved air tank are turned off, and the water making program of the current dissolved air tank is completed.

4. The method for controlling the continuous generation of micro-nano bubbles according to claim 3, characterized in that: The threshold setting for starting the dissolved gas tank switching procedure includes: Obtain the total designed volume of the dissolved air tank, record the time required for the dissolved air tank to be full from the beginning of filling with water, and record the time required for the dissolved air tank to be completely emptied from the beginning of draining water; calculate the average working time of the dissolved air tank; determine the filling and draining rates of the dissolved air tank under normal working conditions, and set a safety margin, which is set at 5% to 10% of the total volume; the triggering filling threshold or draining threshold is the threshold at which the dissolved air tank needs to trigger filling or draining when a certain liquid level is reached, and the threshold is calculated by subtracting the safety margin from the total volume.

5. The method for controlling the continuous generation of micro-nano bubbles according to claim 3, characterized in that: The process of opening the water inlet of the next dissolved air tank includes: Obtain the total opening value between the valve being fully opened and fully closed, the water inlet valve opening value of the current dissolved air tank, and the water inlet valve opening value of the next dissolved air tank; By adjusting the water inlet valves of the current dissolved gas tank and the next dissolved gas tank, the opening of the water inlet valve of the current dissolved gas tank is equal to the difference between the total opening value and the opening value of the next dissolved gas tank; Monitor the water pressure of the water flowing out of the water pump in real time. When the current water pressure value is monitored to be lower than the preset water pressure threshold, continue monitoring. When the current water pressure value is monitored to be higher than the preset water pressure threshold, slow down the closing speed of the current dissolved air tank water inlet valve and speed up the opening speed of the next dissolved air tank water inlet valve until the water pressure is below the preset water pressure threshold.

6. The method for controlling the continuous generation of micro-nano bubbles according to claim 3, characterized in that: The process of starting the ventilation and water discharge functions of the current dissolved air tank includes: Start the water production program, slowly open the ventilation valve of the current dissolved air tank, a one-way valve should be set between the ventilation valve and the dissolved air tank, and collect the opening value of the ventilation valve of the current dissolved air tank in real time; Slowly open the water outlet valve of the current dissolved air tank, and collect the opening value of the water outlet valve of the current dissolved air tank in real time; The flow rate of the micro-nano bubble water outside the water outlet valve is collected in real time, and the collected flow rate data is compared with the preset flow rate interval value. If the collected flow rate value is lower than the interval value, the ventilation valve and the water outlet valve of the current dissolved gas tank will continue to be opened; if the collected flow rate value is within the interval, the current opening of the two valves will be maintained; if the collected flow rate value is higher than the interval value, the opening of the two valves will be slowly reduced until the flow rate value is within the flow rate interval.

7. The method for controlling the continuous generation of micro-nano bubbles according to claim 1, characterized in that: The process of sampling and testing of micro-nano bubble water includes: After the dissolved air tank completes the water production process, the micro-nano bubble water flowing out of the water outlet valve is sampled to detect the particle size and concentration of micron bubbles and nano bubbles respectively; The produced micro-nano bubble water is sampled again and placed in a sample pool to generate its particle size distribution curve and provide statistical information on its average and median particle size; image processing and analysis are performed on the remaining sampled micro-nano bubble water to calculate its bubble volume fraction and concentration; If the obtained particle size data or bubble concentration data is lower than the qualified threshold of micro-nano bubble water, the number and unqualified information of the current dissolved air tank will be displayed through the visualization device, and the staff will be reminded to deal with it in time through the alarm.

8. The method for controlling the continuous generation of micro-nano bubbles according to claim 7, characterized in that: The process of calculating the volume fraction and concentration of bubbles includes: Convert the color image into a grayscale image, use the Canny edge detection algorithm to identify the edges of microbubbles, and identify the connected areas in the image, each of which represents a bubble; The volume of the microbubbles is calculated by the diameter of the detected microbubbles, and the volumes of all detected microbubbles are added together to obtain the total bubble volume; Count the total number of microbubbles detected, record the calculated volume fraction and concentration in a database, and compare the calculated results with the preset qualified threshold; Nanobubbles are detected using an online laser particle size analyzer.

9. A micro-nano bubble continuous generation control system, implementing the micro-nano bubble continuous generation control method according to any one of claims 1 to 8, characterized in that: The micro-nano bubble continuous generation control system comprises: The data acquisition module is responsible for obtaining the number and remaining volume of several dissolved gas tanks, setting the start times of the dissolved gas tank switching program according to the number, and obtaining the remaining volume of the dissolved gas tank by the liquid level sensor; The air dissolving tank switching module, when the remaining volume is equal to the total volume of the current air dissolving tank, the current air dissolving tank forms supersaturated water; the air dissolving tank switching program is started, water is pumped into the new air dissolving tank, and the water inlet of the current air dissolving tank is closed; after the air dissolving tank switching program is completed, the water making program of the current air dissolving tank is started, and the ventilation and release functions are turned on to form micro-nano bubble water; The quality detection module collects the generated micro-nano bubble water and performs sampling detection on it. The samples are taken to detect their particle size distribution and concentration parameters, so as to optimize the bubble generating device.

10. A device for controlling the continuous generation of micro-nano bubbles, implementing the method for controlling the continuous generation of micro-nano bubbles according to any one of claims 1 to 8, characterized in that: The micro-nano bubble continuous generation control device comprises: a water pump, a water inlet valve, a vent valve, a water outlet valve, a first pressure dissolved air tank, a second pressure dissolved air tank, and an nth pressure dissolved air tank; The water pump is connected to the first pressure dissolved gas tank, the second pressure dissolved gas tank and the nth pressure dissolved gas tank through multiple water inlet valves; the top of each pressure dissolved gas tank is connected to the vent valve, and the bottom of each pressure dissolved gas tank is connected to the water outlet valve or the water collection tank.

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