Multifunction integrated salt-chlorine generator

Abstract

The utility model relates to salt chlorine generator technical field, especially in multi -functional integrated type salt chlorine generator, including salt supplement module, electrolytic module, control module and integrated casing, the salt supplement module includes at least the salt bin of salt particle storage and the micro -dosing salt feeder of salt particle delivery and salt guide pipe, is used for the supplement of the storage in the salt bin through micro -dosing salt feeder, the salt bin carries out quantitative unloading through salt guide pipe, the electrolytic module includes electrolytic cavity and sets up on the titanium -based coating electrode group and water circulation pipeline of electrolytic cavity inner wall, the water circulation pipeline is used for introducing water body into electrolytic cavity with salt particle fusion, thereby with titanium -based coating electrode group completes electrolytic reaction in electrolytic cavity. The utility model technical scheme, aims at through integrated design, has improved overall stability and anti -interference ability, and has guaranteed the accurate control of brine concentration and the promotion of electrolytic efficiency.

Description

Technical Field

[0001] This utility model relates to the field of salt chlorine generator technology, and in particular to a multifunctional integrated salt chlorine generator. Background Technology

[0002] With the development of technology and the pursuit of a healthy lifestyle, swimming pools and other water bodies are being used more widely. These water bodies require regular disinfection, such as chlorination, which involves maintaining an appropriate level of residual chlorine in the pool water during use to ensure water quality. Current technology uses salt chlorination generators to ensure stable and automated disinfection.

[0003] Existing salt and chlorine generators mostly adopt a single-function design, requiring separate installation and commissioning of the electrolysis unit, salt replenishment equipment, and water quality testing instruments. This not only occupies a large space but also results in complex piping connections and poor parameter coordination. Traditional equipment lacks an automatic salt replenishment mechanism, requiring frequent manual addition of salt, and the electrodes are prone to calcium and magnesium deposits and scaling, leading to decreased electrolysis efficiency and shortened lifespan. Utility Model Content

[0004] The main purpose of this invention is to provide a multifunctional integrated salt chlorine generator, which aims to improve overall stability and anti-interference ability through integrated design, and to ensure precise control of brine concentration and improved electrolysis efficiency.

[0005] To achieve the above objectives, the present invention proposes a multifunctional integrated salt chlorine generator, comprising:

[0006] The salt replenishment module includes at least a salt bin for storing salt particles, a micro metering salt pump for conveying salt particles, and a salt delivery pipe. It is used to replenish the salt storage in the salt bin through the micro metering salt pump, and the salt bin is fed quantitatively through the salt delivery pipe.

[0007] An electrolysis module, comprising an electrolysis chamber, a titanium-based coated electrode assembly disposed on the inner wall of the electrolysis chamber, and a water circulation pipe, wherein the water circulation pipe is used to introduce water into the electrolysis chamber to fuse with salt particles, thereby completing the electrolysis reaction with the titanium-based coated electrode assembly within the electrolysis chamber;

[0008] The control module includes at least an operation panel and a controller for monitoring and controlling the salt replenishment module and the electrolysis module.

[0009] The integrated housing houses the salt replenishment module, electrolysis module, and control module, while the operation panel is located on the outside of the integrated housing for user convenience.

[0010] In one possible implementation, the bottom of the salt tank is designed with a 15° downward slope to allow salt particles to naturally collect in one place, facilitating monitoring by the control module.

[0011] In one possible implementation, an atomizer is fixedly connected to the salt delivery tube to accelerate the mixing efficiency of the brine.

[0012] In one possible implementation, the electrolysis chamber is provided with a spiral water flow channel to improve the reaction efficiency between the brine and the titanium-based coated electrode assembly.

[0013] In one possible implementation, the control module controls the titanium-based coated electrode assembly to switch a circuit with reverse polarity, the switching circuit being set to a preset period.

[0014] In one possible implementation, a detection chamber is provided at the lower end of the electrolysis chamber, and a diversion pipeline is provided between the detection chamber and the electrolysis chamber. The control module includes a three-in-one sensor for salinity, residual chlorine, and pH. This sensor is used to detect the water in the detection chamber and feed the detection data back to the salt replenishment module and the electrolysis module.

[0015] In one possible implementation, the detection cavity is provided with a baffle.

[0016] In one possible implementation, the control module further includes a protection unit for powering off and alarming in case of equipment failure, and preventing mutual interference between modules.

[0017] This utility model's technical solution integrates the salt replenishment module, electrolysis module, and control module into a compact structure, improving overall stability and anti-interference capabilities. The application of a miniature quantitative salt delivery pump and titanium-coated electrode assembly ensures precise control of brine concentration and improved electrolysis efficiency. The collaborative work of real-time sensors and the control module allows for precise adjustment of salt storage and the electrolysis process, avoiding concentration fluctuations caused by traditional manual operation. The external control panel allows for convenient operation and monitoring, optimizing equipment operability and user experience. The overall design enhances the system's automation and intelligence, ensuring efficient and stable operation of the electrolysis process and simplifying maintenance and management. Attached Figure Description

[0018] To more clearly illustrate the technical solutions in the embodiments of this utility model or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on the structures shown in these drawings without creative effort.

[0019] Figure 1 The structural frame of this utility model is a multifunctional integrated salt chlorine generator. Figure 1 ;

[0020] Figure 2 The structural frame of this utility model is a multifunctional integrated salt chlorine generator. Figure 2 ;

[0021] Figure 3 This is a schematic diagram of the multifunctional integrated salt chlorine generator of this utility model;

[0022] Figure 4 This is a partial cross-sectional view of the multifunctional integrated salt chlorine generator of this utility model. Figure 1 ;

[0023] Figure 5 This is a partial cross-sectional view of the multifunctional integrated salt chlorine generator of this utility model. Figure 2 ;

[0024] Figure 6 This is a partial cross-sectional view of the multifunctional integrated salt chlorine generator of this utility model. Figure 3 ;

[0025] Figure 7 This is a partial cross-sectional view of the multifunctional integrated salt chlorine generator of this utility model. Figure 4 .

[0026] The realization of the purpose, functional features and advantages of this utility model will be further explained in conjunction with the embodiments and with reference to the accompanying drawings.

[0027] Explanation of icon numbers:

[0028] 11. Salt tank; 12. Miniature quantitative salt delivery pump; 13. Salt delivery pipe; 21. Electrolysis chamber; 22. Titanium-based coated electrode assembly; 23. Water circulation pipe; 31. Operation panel; 32. Controller; 4. Integrated housing; 5. Detection chamber. Detailed Implementation

[0029] To make the objectives, technical solutions, and advantages of this application clearer, the following detailed description is provided in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative and not intended to limit the scope of this application.

[0030] This utility model proposes a multifunctional integrated salt and chlorine generator.

[0031] Example 1

[0032] Reference Figures 1 to 7 The system includes a salt replenishment module, which includes at least a salt bin 11 for storing salt particles, a micro quantitative salt delivery pump 12 for conveying salt particles, and a salt guide pipe 13. The module is used to replenish the salt storage in the salt bin 11 through the micro quantitative salt delivery pump 12, and the salt bin 11 is fed quantitatively through the salt guide pipe 13.

[0033] The salt replenishment module is designed with a salt tank 11, a micro-metering salt pump 12, and a salt delivery pipe 13 to achieve efficient and precise salt replenishment. The micro-metering salt pump 12, through precise control, ensures that salt particles in the salt tank 11 are delivered quantitatively as needed, avoiding the addition of too much or too little salt particles, significantly improving the stability of salt replenishment, and thus ensuring a consistent brine concentration during electrolysis. This design allows the electrolysis reaction to proceed at the optimal salt concentration, effectively improving reaction efficiency and avoiding energy loss due to concentration fluctuations.

[0034] In addition, sensors on the lower side of the salt tank 11 monitor the salt particle level inside the tank in real time and transmit the data to the control module. The control module preferably uses an MCU controller 32, which is a microcontroller and serves as the embedded computing center, processing the monitoring data. The operating current is typically in the mA range, supporting 12V / 5V DC power supply, and can even be backed up with a lithium battery, fully meeting the requirements of the small salt tank 11 for "long standby time and no need for frequent power supply maintenance".

[0035] The built-in interface receives 4-20mA signals from the load cell and 0-10V signals from the capacitive probe via the analog input port; and receives dry contact signals from the rotary paddle level switch via the digital input port. All signals are processed directly through the built-in interface without the need for intermediate conversion equipment.

[0036] The algorithm of "zero-point compensation + linear calibration" is used to convert the raw digital quantity collected by the ADC into the actual salt quantity (kg). The real-time salt quantity is compared with the preset threshold (5kg for low material level, 20kg for full silo, etc.) to trigger the corresponding control logic (start salt replenishment, stop salt replenishment, alarm).

[0037] The salt storage in the salt tank 11 is precisely replenished by driving a miniature quantitative salt pump 12. The sensor under the salt tank 11 is preferably a weight sensor or other small load-bearing module. It is first calibrated using a standard salt sample to establish a calibration curve between the sensor response value and the actual salt quantity. During operation, the sensor detects the weight of the salt particles in real time and transmits a 4-20mA analog signal to the control module. The controller 32 in the control module compares the detected value with a preset threshold.

[0038] Specifically, the change in the weight of the salt grains causes a small deformation to the supporting structure on the lower side. This deformation data is converted into a millivolt-level analog signal, which is then processed by a signal amplifier and an analog-to-digital converter to output a 4-20mA standard signal or an RS485 digital signal to the controller 32.

[0039] The micro salt delivery pump can be a peristaltic pump or a small screw pump, which are suitable for conveying particulate media. The pump body is interlocked with the controller 32. When the controller 32 receives a digital signal, it provides feedback to the pump body and opens the inlet valve of the salt bin 11.

[0040] The pump's delivery rate can be adjusted by the controller 32, which can regulate the speed or stroke. The salt bin 11 can be replenished according to a preset threshold. For example, when the salt level in the salt bin 11 is lower than the threshold, the pump can replenish the salt to that threshold. Once the level is close to the threshold, the pump's speed or stroke will gradually slow down until it aligns with the threshold. Then, a signal will be sent to the orifice. After receiving the signal, the controller 32 will issue a stop command to stop the micro salt pump and close the valve at the inlet of the salt bin 11, completing one salt replenishment cycle. The controller can also adjust the threshold in the salt bin 11 during the salt replenishment process and based on the digital signals fed back from the electrolysis module, ensuring more accurate salt delivery.

[0041] This automated control method avoids the errors and concentration fluctuations of traditional manual salt replenishment, ensuring system stability and continuous optimization of the reaction process. This technical solution not only improves the accuracy of the salt replenishment process but also effectively reduces manual intervention, lowering operational risks and maintenance costs, thereby enhancing the overall system's operational efficiency and reliability.

[0042] When the salt level sensor detects that the salt level in the salt tank 11 is lower than the set threshold, the MCU controller 32 starts the micro salt delivery pump to add salt at a dose of 0.5g per liter of water. The pump automatically stops after the salt replenishment is completed.

[0043] An electrolysis module, comprising an electrolysis chamber 21, a titanium-based coated electrode assembly 22 disposed on the inner wall of the electrolysis chamber 21, and a water circulation pipe 23, wherein the water circulation pipe 23 is used to introduce water into the electrolysis chamber 21 to fuse with salt particles, thereby completing the electrolysis reaction with the titanium-based coated electrode assembly 22 in the electrolysis chamber 21.

[0044] The electrolysis module employs a titanium-coated electrode assembly 22, coupled with a water circulation pipeline system 23. Water is introduced into the electrolysis chamber 21 and mixed with salt particles fed through the salt inlet pipe 13 to form a dilute brine. This dilute brine, precisely replenished by the salt replenishment tank 11, allows for precise concentration control, enabling it to work in conjunction with the titanium-coated electrode assembly 22 to complete the electrolysis reaction. Due to its excellent corrosion resistance and electrical conductivity, the titanium-coated electrode assembly 22 not only significantly improves electrolysis efficiency but also effectively extends the electrode's lifespan and reduces maintenance frequency.

[0045] The titanium-based coated electrode assembly 22 uses a titanium-based composite iridium-ruthenium coating. The reverse polarity switching circuit starts a cleaning program every 8 hours of operation, with each reverse power-on lasting 30 seconds.

[0046] The design of the water circulation pipe 23 optimizes the mixing effect of water flow and salt particles, allowing the salt particles to dissolve more evenly in the water, thereby improving the efficiency and stability of the electrolysis reaction. Through good water flow control, the dilute brine can maintain a constant concentration, ensuring that the chemical reaction during the electrolysis process proceeds under optimal conditions.

[0047] The control module includes at least an operation panel 31 and a controller 32 for monitoring and controlling the salt replenishment module and the electrolysis module.

[0048] The control module design, through the collaborative operation of the operation panel 31 and the controller 32, achieves precise monitoring and control of the salt replenishment module and the electrolysis module, ensuring the intelligent and automated operation of the entire system. Users can conveniently adjust system parameters, view the working status in real time, and optimize the system's operating efficiency through the operation panel 31.

[0049] Controllers 32 are located at the outlet of salt tank 11 and the electrolysis chamber 21, respectively. They monitor data in real time and feed it back to the control module to ensure coordination and cooperation between the modules. When the electrolysis efficiency changes or other concentration problems occur during electrolysis, the control module will adjust the salt supply of salt tank 11 and the electrical charge on the wall of electrolysis chamber 21 according to user needs, thereby maintaining the optimal concentration of dilute brine and ensuring the stability and efficiency of the electrolysis reaction.

[0050] The flow rate of the diversion pipeline is 10%-15% of the main flow rate of the electrolysis chamber 21. The baffle plate ensures that the water sample is mixed evenly. The sensor data is transmitted to the control module every 5 seconds. The input voltage range of the power supply circuit is AC220V±10%. The MCU controller 32 adjusts the electrolysis current range to 0.5-5A according to the monitoring data to ensure that the residual chlorine concentration is maintained at 0.3-0.5mg / L.

[0051] The integrated housing 4 houses the salt replenishment module, electrolysis module, and control module, while the operation panel 31 is located on the outside of the integrated housing 4 for user convenience.

[0052] The integrated housing 4 tightly encapsulates the salt replenishment module, electrolysis module, and control module within a unified structure, ensuring the system's compactness and stability. By effectively integrating these modules, mutual interference between internal components is reduced, and the impact of external environmental factors on the equipment is effectively prevented, thereby improving the equipment's durability and operational reliability. This design not only optimizes space utilization but also enhances the overall system's structural strength, preventing loosening or other mechanical problems and strengthening the equipment's anti-interference capabilities.

[0053] Through integrated design, the salt replenishment module, electrolysis module, and control module are compactly packaged into a single structure, improving overall stability and anti-interference capabilities. The application of the miniature quantitative salt delivery pump 12 and the titanium-coated electrode assembly 22 ensures precise control of brine concentration and improved electrolysis efficiency. The collaborative operation of real-time sensors and the control module allows for precise adjustment of the salt tank 11's storage capacity and the electrolysis process, avoiding concentration fluctuations caused by traditional manual operation. The external operation panel 31 allows for convenient operation and monitoring, optimizing equipment operability and user experience. The overall design enhances the system's automation and intelligence levels, ensuring efficient and stable operation of the electrolysis process and simplifying maintenance and management.

[0054] It should be noted that under the influence of an electric field, salt water undergoes an electrolysis reaction: chloride ions (Cl-) are present at the anode. - At the cathode, water molecules (H2O) lose electrons to produce chlorine gas (Cl2), while water molecules gain electrons to produce hydrogen gas (H2) and hydroxide ions (OH-). - Chlorine reacts further with hydroxide ions to produce sodium hypochlorite, a disinfectant with strong oxidizing properties. The overall reaction equation is NaCl + H₂O → NaClO + H₂↑.

[0055] The water containing sodium hypochlorite generated by electrolysis is discharged through the outlet and enters the swimming pool and storage tank to wait for disinfection. Sodium hypochlorite hydrolyzes to produce hypochlorous acid (HCLO), which sterilizes and disinfects by destroying the protein structure and nucleic acid chain of microorganisms such as bacteria and algae.

[0056] According to Figures 1 to 2 The control module controls the titanium-based coated electrode group 22 to switch the circuit in reverse polarity, and the switching circuit is set with a preset period.

[0057] The control module uses a reverse polarity switching circuit to switch the positive and negative electrodes at a preset cycle (every 8 hours by default). This reverse current dissolves the calcium and magnesium scale deposited on the electrode surface, allowing it to be discharged through the water, thus extending the electrode's lifespan and ensuring effective electrolysis of the subsequent water.

[0058] Reference Figures 1 to 2 The lower end of the electrolysis chamber 21 is provided with a detection chamber 5. A diversion pipeline is provided between the detection chamber 5 and the electrolysis chamber 21. The control module includes a three-in-one sensor for salinity, residual chlorine and pH. This sensor is used to detect the water in the detection chamber 5 and feed the detection data back to the salt replenishment module and the electrolysis module.

[0059] The detection chamber 5 located at the lower end of the electrolysis chamber 21 is equipped with a three-in-one sensor for salinity, residual chlorine, and pH. This sensor monitors relevant water data in real time and feeds the data back to the salt replenishment module and the electrolysis module via the control module. This allows for control of the salt feed in the salt replenishment module and the electrolysis charge in the electrolysis module. This design precisely controls salinity changes during electrolysis and automatically adjusts the salt replenishment amount or electrolysis conditions when necessary, ensuring that the water quality remains within a suitable range.

[0060] A three-in-one sensor for salinity, residual chlorine, and pH collects data every 5 seconds, which is then converted and transmitted to the MCU controller 32. The controller 32 compares the monitored data with pre-stored thresholds (such as residual chlorine 0.3-0.5 mg / L and pH 7.2-7.8), and dynamically adjusts the electrolysis current (0.5-5 A) and the brine pump flow rate to achieve a closed-loop control of "detection-feedback-adjustment" to ensure that water quality parameters remain stable within a safe range.

[0061] In addition, a one-way valve should be added at the connection between the detection chamber 5 and the electrolysis chamber 21 to prevent backflow of the detection solution and ensure the accuracy of water body detection.

[0062] Reference Figures 1 to 2 The control module also includes a protection unit for powering off and alarming in case of equipment failure, and for preventing mutual interference between modules.

[0063] The protection unit in the control module can promptly cut off power and issue an alarm when a device malfunctions, preventing the system failure from spreading and affecting the normal operation of other modules. This protection function ensures the safety and reliability of the equipment and reduces downtime or losses caused by malfunctions.

[0064] Specifically, the protection unit primarily targets the electrolysis chamber 21 based on the brine concentration, and also provides protection and early warning against overall equipment leakage, pressure relief, and pipeline failures.

[0065] Regarding the saline concentration, the conductivity sensor in the protection unit outputs a 4-20mA analog signal to the MCU controller 32, which presets the "lower concentration threshold (corresponding to 2% NaCl, conductivity = 22mS / cm)" and the "upper concentration threshold (corresponding to 3% NaCl, conductivity = 33mS / cm)".

[0066] When the detected conductivity is <22 mS / cm (concentration below 2%, insufficient electrolysis efficiency): MCU controller 32 immediately triggers the start of the salt replenishment pump (speed adjusted to 80% of rated speed to avoid excessive salt replenishment leading to a sudden increase in local concentration). Simultaneously, the electromagnetic three-way valve is opened, and the salt particles enter the electrolysis chamber 21 through the salt guide pipe 13, mixing with the water discharged from the circulating water pipe and dissolving to form a salt solution. During the salt replenishment process, conductivity data is collected every second. When the conductivity reaches 2.5%-2.7% (corresponding to 27.5-29.7 mS / cm, the middle concentration range, ensuring stability), the salt replenishment pump is reduced to 30% of the rated speed (tricooking salt replenishment mode). Salt replenishment continues until the conductivity reaches 28-30 mS / cm (corresponding to 2.55%-2.73%), at which point the salt replenishment pump is stopped and the electromagnetic three-way valve is closed to prevent the concentration from approaching the upper limit threshold.

[0067] When the detected conductivity is >33 mS / cm (concentration higher than 3%, excessive disinfectant): MCU controller 32 immediately shuts off the salt replenishment pump and the solenoid three-way valve, while simultaneously starting the diluent replenishment pump to inject clean water to dilute the salt solution; during the dilution process, conductivity is collected every 0.5 seconds. When the conductivity drops to 28-30 mS / cm (corresponding to 2.55%-2.73%), the diluent replenishment pump is shut off, and the electrolysis reaction resumes; if the conductivity is still >33 mS / cm after 5 minutes of dilution, "E01: Concentration Exceeds Standard Alarm" (audio-visual prompt + remote push) is triggered, prompting the user to check whether the salt replenishment pump is stuck or whether the diluent channel is blocked.

[0068] For equipment leaks, pressure drops, and pipeline malfunctions, a multi-point leak detection cable is used, preferably over 2m in length for easy cutting. It is installed along the bottom edge of the integrated housing 4, and laid around the salt guide pipe 13 between the electrolysis chamber 21 and the salt tank 11, as well as around the location where the circulating pipe and the electrolysis chamber 21 flow into the external water body. Then, a leak detection module integrating signal amplification and comparator is installed in series with the leak detection cable. Finally, a drainage pump is installed at the bottom of the integrated housing 4, and a warning indicator light is installed on the outside of the integrated housing 4 to provide warning through light color.

[0069] The leak detection cable is made of conductive polymer material and is in a high-resistance state (≥10MΩ) under normal conditions. When salt solution, clean water or condensate seeps into the cable surface, the cable becomes locally conductive and the resistance drops sharply to ≤1kΩ. The leak detection module immediately outputs a low-level switch signal to the MCU controller 32.

[0070] After receiving the signal, the MCU triggers a level-three protection action within 100ms;

[0071] Cut off the sources of risk: shut down the salt replenishment pump, diluent supply pump, and power supply to electrolysis chamber 21 to prevent further leakage;

[0072] Active drainage: Activate the emergency drainage pump to pump the leaking liquid in the water collection groove to the external waste liquid tank (which needs to be placed by the user). The drainage pump will continue to run until the leakage detection signal disappears, and then shut off after a 30-second delay.

[0073] Alarm feedback: Triggers local audible and visual alarm (yellow water leakage indicator flashes, frequency 2 times / second + intermittent buzzer sound), and simultaneously pushes "E09: Equipment water leakage alarm" remotely, along with the approximate leakage area of ​​the water leakage detection cable (determined by the segmented resistance of the cable);

[0074] If the leakage signal does not disappear after the drainage pump has been running for 5 minutes, the MCU will determine that there is a serious leak and cut off the power supply to the whole machine (except for the alarm module). The user needs to manually check the leak point (such as loose pipe joints or aging of the sealing gasket of electrolysis chamber 21) and clean it before pressing the reset button to restore the power supply.

[0075] It is worth noting that the hardware trigger actions of external protection (such as hardware power-off when there is a water leak, and relay tripping when there is an overcurrent) have higher priority than internal protection, ensuring that external risks are blocked first in an emergency. All status signals of the external protection module (such as water leak detection and current / voltage data) are uploaded to the MCU in real time and stored together with the internal protection data. The fault record includes "external anomaly type + internal operating conditions at the time of triggering" (such as brine concentration and electrolysis current when there is a water leak), which is convenient for troubleshooting.

[0076] Example 2

[0077] This embodiment improves the shape of the inner wall of the salt tank 11 based on the previous embodiment;

[0078] Reference Figures 1 to 7 The bottom of the salt tank 11 is designed with a 15° downward tilt to allow the salt particles to naturally collect in one place, making it convenient for the control module to monitor them.

[0079] The 15° inclined structure at the bottom of the salt bin 11 helps the salt particles to naturally gather in one place. This allows the salt particles in the salt bin 11 to naturally gather in the detection area of ​​the salt quantity sensor, enabling the control module to monitor the storage level in the salt bin 11 in real time and thus drive the salt replenishment module. At the same time, the inclined structure at the bottom of the salt bin 11 prevents the salt particles from accumulating in the salt bin 11 for a long time and becoming damp, thereby reducing the salt particle concentration and ensuring stable feeding of salt particles. This prevents the same batch of salt particles from being stored in the salt bin 11 for a long time and prevents multiple batches of salt particles from being mixed, thus reducing the difficulty in controlling the accuracy of salt particle feeding.

[0080] Example 3

[0081] This embodiment improves upon the mixing effect of brine based on Embodiment 1;

[0082] Reference Figures 1 to 7An atomizer is fixedly connected to the salt guide tube 13 to accelerate the mixing efficiency of the brine.

[0083] Fixing an atomizer on the salt delivery tube 13 accelerates the mixing efficiency of the brine, rapidly dissolving the salt particles and distributing them evenly throughout the water. This design helps improve the efficiency of the electrolysis reaction, preventing salt particles from settling or dissolving incompletely in the water, thereby enhancing the overall effectiveness of the brine electrolysis process.

[0084] Example 4

[0085] This embodiment improves upon the efficiency of the electrolysis reaction based on Example 1;

[0086] Reference Figure 7 The electrolysis chamber 21 is provided with a spiral water flow channel to improve the reaction efficiency of brine with the titanium-based coated electrode assembly 22.

[0087] The spiral water flow channel within the electrolysis chamber 21 effectively increases the contact area between the brine and the titanium-coated electrode assembly 22. By increasing the water flow and residence time within the electrolysis chamber 21, the water can better contact the titanium-coated electrode assembly 22, thereby achieving a more stable electrolysis reaction and optimizing its efficiency. Furthermore, the spiral guidance of the water within the electrolysis chamber 21 ensures more uniform mixing, prevents the precipitation of particulate matter, and results in a more uniform concentration within the water, further improving the electrolysis effect.

[0088] Furthermore, it ensures that the water uniformity remains stable when the water flows to the detection chamber 5.

[0089] This design not only ensures a more stable electrolysis reaction and enhances electrolysis efficiency, but also improves the mixing effect of the water, making the electrolyzed water mix more evenly and further improving the electrolysis effect of the water.

[0090] Example 5

[0091] This embodiment improves upon Embodiment 1 on the mixing effect of the water in the detection chamber 5;

[0092] Reference Figures 1 to 7 The detection cavity 5 is equipped with a baffle.

[0093] The mixed water entering the detection chamber 5 through the diversion pipe is further mixed to achieve the most uniform concentration, facilitating detection by the combined salinity, residual chlorine, and pH sensor. Simultaneously, the baffles within detection chamber 5 improve the flow pattern, preventing dead zones and enhancing the contact efficiency between the water and the sensor. This design facilitates the mixing of the monitored water and more accurately monitors water quality changes, ensuring accurate and reliable data and further optimizing the overall system operation.

[0094] In the accompanying drawings of this embodiment, the same or similar reference numerals correspond to the same or similar components. In the description of this application, it should be understood that if terms such as "upper," "lower," "left," and "right" indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, they are only for the convenience of describing this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, the terms used to describe positional relationships in the accompanying drawings are only for illustrative purposes and should not be construed as limiting this patent. For those skilled in the art, the specific meaning of the above terms can be understood according to the specific circumstances.

[0095] The above are merely preferred embodiments of this application and are not intended to limit this application. Any modifications, equivalent substitutions, and improvements made within the spirit and principles of this application should be included within the protection scope of this application.

Claims

1. A multi-functional integrated salt chlorine generator, characterized in that, include: The salt replenishment module includes at least a salt bin (11) for storing salt particles, a micro quantitative salt delivery pump (12) for conveying salt particles, and a salt guide pipe (13). It is used to replenish the storage in the salt bin (11) through the micro quantitative salt delivery pump (12), and the salt bin (11) is quantitatively fed through the salt guide pipe (13). An electrolysis module, comprising an electrolysis chamber (21), a titanium-based coated electrode assembly (22) disposed on the inner wall of the electrolysis chamber (21), and a water circulation pipe (23), wherein the water circulation pipe (23) is used to introduce water into the electrolysis chamber (21) to fuse with salt particles, thereby completing the electrolysis reaction with the titanium-based coated electrode assembly (22) in the electrolysis chamber (21); The control module includes at least an operation panel (31) and a controller (32) for monitoring and controlling the salt replenishment module and the electrolysis module; The integrated housing (4) contains the salt replenishment module, the electrolysis module and the control module, and the operation panel (31) is located on the outside of the integrated housing (4) for user convenience.

2. The multifunctional integrated salt chlorine generator according to claim 1, characterized in that, The bottom of the salt tank (11) is designed with a 15° downward tilt to allow salt particles to naturally collect in one place, making it convenient for the control module to monitor them.

3. The multifunctional integrated salt chlorine generator according to claim 1, characterized in that, An atomizer is fixedly connected to the salt guide tube (13) to accelerate the mixing efficiency of the brine.

4. The multifunctional integrated salt chlorine generator according to claim 1, characterized in that, The electrolysis chamber (21) is provided with a spiral water flow channel to improve the reaction efficiency of brine with the titanium-based coated electrode assembly (22).

5. The multifunctional integrated salt chlorine generator according to claim 1, characterized in that, The control module controls the titanium-based coated electrode group (22) to switch the circuit in reverse polarity, and the switching circuit is set with a preset period.

6. The multifunctional integrated salt chlorine generator according to claim 5, characterized in that, The lower end of the electrolysis chamber (21) is provided with a detection chamber (5), and a diversion pipeline is provided between the detection chamber (5) and the electrolysis chamber. The control module includes a three-in-one sensor for salinity, residual chlorine and pH. The sensor is used to detect the water in the detection chamber and feed back the detection data to the salt replenishment module and the electrolysis module.

7. The multifunctional integrated salt chlorine generator according to claim 6, characterized in that, The detection chamber is equipped with a baffle.

8. The multifunctional integrated salt chlorine generator according to claim 1, characterized in that, The control module also includes a protection unit, which is used to cut off power and issue alarms in case of equipment failure, and to prevent mutual interference between modules.

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