Electrolysis machine

Abstract

The utility model relates to the technical field of metal extraction, and discloses an electrolysis machine which comprises a carrier plate, an electrolytic tank is fixedly connected to the front side of the top of the carrier plate, a positive conductive plate is fixedly connected to the rear side in the electrolytic tank, and a plurality of negative plates penetrate through the top of the front side of the electrolytic tank at equal intervals. Battery cells are fixedly connected to the front ends of the bottoms of the multiple negative plates, mounting grooves are formed in the rear sides of the tops of the multiple negative plates, negative metal bars penetrate through the interiors of the multiple mounting grooves, and fixed circular plates are fixedly connected to the middle upper parts of the multiple negative metal bars. According to the utility model, the anode current-conducting plate and the cathode plate respectively form an anode and a cathode after being electrified, and the current on the other side is conducted to the plurality of cathode metal bars through the cathode plate, so that precious metal is extracted from a solution containing precious metal ions, the reaction area is greatly increased, the electrode connection is stabilized, and the electrolysis condition is accurately controlled; the reaction rate and the resource recycling rate are improved.

Description

Technical Field

[0001] This utility model relates to the field of metal extraction technology, and in particular to an electrolysis machine. Background Technology

[0002] An electrolytic cell is a device that uses the principle of electrolysis to extract precious metals. Electrolysis refers to the process in which cations and anions in an electrolyte solution or molten electrolyte undergo oxidation-reduction reactions on the electrodes under the action of an electric current. For the extraction of precious metals, by rationally designing the electrolytic cell and selecting electrode materials, the target precious metal can be deposited on the electrodes, thereby achieving separation from other impurities.

[0003] A search revealed Chinese patent publication number CN215251235U, which discloses an electrolytic gold extraction machine, relating to metal refining equipment. The machine includes an electrolytic cell for holding the liquid to be refined, an anode assembly, and a cathode assembly, both of which are disposed within the electrolytic cell. It also includes a storage tank for holding the liquid, the height of which is lower than the height of the electrolytic cell. An inlet pipe connects the electrolytic cell and the storage tank, allowing the liquid in the storage tank to flow into the electrolytic cell. A water pump is connected to the inlet pipe. An outlet pipe also connects the electrolytic cell and the storage tank, returning the liquid from the electrolytic cell to the storage tank. This design improves the electrolytic efficiency of gold extraction. However, this equipment requires an additional storage tank and associated inlet, outlet, and water pump, increasing costs and maintenance difficulty. Furthermore, the liquid circulation relies on the water pump, and the circulation of the electrolyte within the pump can corrode it, increasing the likelihood of malfunction and affecting the electrolysis process. Utility Model Content

[0004] To overcome the above deficiencies, this utility model provides an electrolysis machine, which aims to improve the problem in the prior art where the electrolyte circulates inside the water pump, causing corrosion to the water pump and increasing the possibility of failure, thereby affecting the electrolysis process.

[0005] To achieve the above objectives, the present invention adopts the following technical solution: an electrolyzer, comprising a carrier plate, an electrolytic cell fixedly connected to the top front side of the carrier plate, a positive electrode conductive plate fixedly connected to the inner rear side of the electrolytic cell, a plurality of negative electrode plates equidistantly penetrating the top front side of the electrolytic cell, a battery cell fixedly connected to the bottom front end of each of the plurality of negative electrode plates, an installation groove provided on the top rear side of each of the plurality of negative electrode plates, a negative electrode metal rod penetrating inside each of the plurality of installation grooves, a fixed circular plate fixedly connected to the upper middle part of each of the plurality of negative electrode metal rods, the plurality of fixed circular plates respectively engaging with the plurality of installation grooves, and a solution turbulence mechanism provided on the top rear side of the carrier plate.

[0006] The above technical solution involves using an electrolytic cell to contain electrolyte. After being energized, the positive electrode plate and the negative electrode plate form the anode and cathode, respectively. Multiple battery cells supply power so that the current is conducted through the negative electrode plate to multiple negative electrode metal rods. This achieves efficient extraction of precious metals from solutions containing precious metal ions, greatly increases the reaction area, stabilizes electrode connections, and precisely controls electrolysis conditions, thereby improving the reaction rate and resource recovery rate.

[0007] As a further description of the above technical solution:

[0008] The solution turbulence mechanism includes a booster, the bottom of which is fixedly connected to the left rear end of the top of the carrier plate. A pressure stabilizing tank is fixedly connected to the output end of the booster, and the bottom of the pressure stabilizing tank is fixedly connected to the right rear end of the top of the carrier plate. A partition is fixedly connected to the center of the inside of the pressure stabilizing tank, and a pressure regulator is fixedly installed in the middle of the partition. A high-pressure chamber is arranged on the left side of the inside of the pressure stabilizing tank, and a pressure stabilizing chamber is arranged on the right side of the inside of the pressure stabilizing tank. A conduit is connected to the right end of the pressure stabilizing tank, and an electrically controlled valve is fixedly installed in the middle of the conduit. A diversion pipe is connected to the output end of the conduit, and multiple nozzles are fixedly installed at equal intervals on the top of the diversion pipe. The tops of the multiple nozzles penetrate the inner bottom wall of the electrolytic cell.

[0009] The above technical solution involves using a booster to compress gas and send it into a pressure stabilizing tank. After the pressure is balanced by a pressure regulator, the gas is sprayed into the electrolytic cell through a nozzle via a conduit. This improves the fluidity and uniform distribution of the electrolyte, making the current conduction between the electrodes smoother, reducing current conduction resistance, increasing current density, accelerating the electrolytic reaction rate, and significantly increasing the deposition rate of precious metal ions on the electrodes. Ultimately, this improves the efficiency of the electrolytic machine in extracting precious metals.

[0010] As a further description of the above technical solution:

[0011] A mounting frame is fixedly connected to the top left side of the carrier plate, and a crusher is fixedly installed inside the mounting frame.

[0012] Through the above technical solution, the crusher inside the mounting frame can compress larger pieces of material into smaller pieces, which increases the surface area of ​​the material, allowing it to come into more full contact with the electrolyte when it enters the electrolytic cell for electrolysis, thereby improving the efficiency of precious metal extraction.

[0013] As a further description of the above technical solution:

[0014] A control console is fixedly connected to the front right end of the electrolytic cell, and multiple control buttons are fixedly connected to the top of the control console.

[0015] Through the above technical solution: the control console is the central hub of the entire electrolysis machine, and the control buttons on its top are used to adjust the current intensity during the electrolysis process, thereby controlling the rate of the electrolysis reaction by changing the current magnitude.

[0016] As a further description of the above technical solution:

[0017] A voltmeter is fixedly connected to the middle of the front side of the electrolytic cell, and the voltmeter is electrically connected to the positive electrode conductive plate.

[0018] Through the above technical solution, the voltmeter can monitor the voltage across the positive electrode conductive plate in real time during the electrolysis process in the electrolytic cell. The voltage value displayed by the voltmeter can be used to intuitively understand the current voltage state of the electrolysis reaction, so as to detect abnormal voltage conditions in a timely manner.

[0019] As a further description of the above technical solution:

[0020] A drain pipe is connected to the bottom right side of the electrolytic cell, and a valve is fixedly installed on the top of the drain pipe.

[0021] The above technical solution allows the drain pipe to discharge the electrolyte from the electrolytic cell when needed. By adjusting the opening of the valve at the top, the discharge rate of the electrolyte can be precisely controlled to meet different operational requirements.

[0022] As a further description of the above technical solution:

[0023] A placement rack is fixedly installed on the lower part of the inner wall of the electrolytic cell. The placement rack is made of non-conductive material.

[0024] The above technical solution involves fixing the rack to the lower part of the inner wall of the electrolytic cell and using a non-conductive material. This effectively prevents short circuits between the items placed on it and the electrodes, ensuring the safe operation of the electrolytic machine and the normal progress of the electrolytic reaction.

[0025] As a further description of the above technical solution:

[0026] Each of the multiple negative electrode metal rods has an extraction ring fixedly connected to its top, and the exterior of each of the multiple extraction rings is treated with a frosting process.

[0027] The above technical solution allows for easy handling of the negative electrode metal rod, improving the convenience and efficiency of precious metal extraction.

[0028] This utility model has the following beneficial effects:

[0029] 1. In this utility model, an electrolytic cell contains an electrolyte, and the positive electrode conductive plate and the negative electrode plate form the anode and cathode respectively after being energized. Multiple battery cells supply power so that the current is conducted through the negative electrode plate to multiple negative electrode metal rods, thereby realizing the efficient extraction of precious metals from solutions containing precious metal ions, greatly increasing the reaction area, stabilizing electrode connections and precisely controlling electrolysis conditions, and improving the reaction rate and resource recycling rate.

[0030] 2. In this utility model, the gas is compressed by a booster and sent into a pressure stabilizing tank. After the pressure is balanced by a pressure regulator, the gas is sprayed into the electrolytic cell through a nozzle via a conduit. This improves the fluidity and uniform distribution of the electrolyte, makes the current conduction between the electrodes smoother, reduces the current conduction resistance, increases the current density, accelerates the electrolytic reaction rate, and significantly increases the deposition rate of precious metal ions on the electrodes, ultimately improving the efficiency of the electrolytic machine in extracting precious metals. Attached Figure Description

[0031] Figure 1 This is a perspective view of an electrolysis machine proposed in this utility model;

[0032] Figure 2 This is a front view of an electrolysis machine proposed in this utility model;

[0033] Figure 3 This is a top view of an electrolysis machine proposed in this utility model;

[0034] Figure 4 This is a cross-sectional view of a pressure stabilizing tank in an electrolyzer according to the present invention;

[0035] Figure 5 This is a structurally exploded view of the negative electrode metal rod in an electrolytic machine proposed in this utility model.

[0036] Legend:

[0037] 1. Carrier plate; 2. Electrolytic cell; 3. Positive conductive plate; 4. Negative plate; 5. Cell; 6. Mounting slot; 7. Negative metal rod; 8. Fixing circular plate; 9. Booster; 10. Pressure stabilizing tank; 11. Partition plate; 12. Pressure regulator; 13. High-pressure chamber; 14. Pressure stabilizing chamber; 15. Conduit; 16. Electrically controlled valve; 17. Diverter pipe; 18. Nozzle; 19. Mounting frame; 20. Crusher; 21. Control console; 22. Control button; 23. Voltmeter; 24. Drain pipe; 25. Valve; 26. Placement rack; 27. Extraction ring. Detailed Implementation

[0038] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0039] Reference Figure 1 , Figure 3 and Figure 5 This utility model provides an embodiment of an electrolytic machine, including a carrier plate 1. An electrolytic cell 2 is fixedly connected to the front top of the carrier plate 1, providing a stable container base for the electrolytic reaction and ensuring the stability of the electrolytic cell 2 during operation. A positive electrode conductive plate 3 is fixedly connected to the rear inside of the electrolytic cell 2, serving as the anode to participate in the electrolytic reaction and providing a site for the oxidation reaction, allowing metal ions to lose electrons and dissolve into the electrolyte when electricity is applied. Multiple negative electrode plates 4 are equidistantly penetrating the top front side of the electrolytic cell 2, increasing the reaction area and improving electrolysis efficiency. Battery cells 5 are fixedly connected to the front bottom of each of the multiple negative electrode plates 4, providing electrical energy to the entire electrolysis system and ensuring the stability of the electrolytic reaction. To ensure the necessary power supply, mounting grooves 6 are provided on the top and rear sides of multiple negative electrode plates 4 to facilitate the installation and positioning of negative electrode metal rods 7. The negative electrode metal rods 7 penetrate through the interior of multiple mounting grooves 6, which can effectively conduct the current of the cell 5 to the negative electrode plate 4. Fixed circular plates 8 are fixedly connected to the upper middle part of multiple negative electrode metal rods 7. The multiple fixed circular plates 8 are respectively engaged with multiple mounting grooves 6 to ensure the stability of the connection between the negative electrode metal rods 7 and the negative electrode plate 4, and to avoid loosening during the electrolysis process, which would affect the current conduction. A solution tumbling mechanism is provided on the top and rear side of the carrier plate 1. This mechanism can improve the fluidity and uniform distribution of the electrolyte, thereby increasing the current density and promoting a more efficient electrolysis reaction.

[0040] Specifically, the electrolytic cell 2 at the top of the carrier plate 1 is the core container for the electrolytic reaction. The positive electrode conductive plate 3, fixedly connected to the rear side inside the electrolytic cell 2, becomes the anode after energization, undergoing an oxidation reaction. Multiple negative electrode plates 4 are equidistantly connected to the front top of the electrolytic cell 2. The battery cells 5, fixedly connected to the bottom front of these negative electrode plates 4, primarily provide electrical energy, forming a closed loop in the entire electrolytic system. When the circuit is connected, current is conducted to the negative electrode plates 4 through the negative electrode metal rod 7. The mounting groove 6 on the rear side of the top of the electrode plate 4 is connected to the mounting groove 6 by a fixed circular plate 8, thus achieving a stable connection and ensuring that the current can smoothly flow from the cell 5 through the negative electrode metal rod 7 to the negative electrode plate 4. In the electrolyte containing noble metal ions, after energization, the positive electrode conductive plate 3 of the anode will undergo an oxidation reaction, causing the metal ions to lose electrons and dissolve into the electrolyte. At the cathode, i.e., the negative electrode plate 4, the noble metal ions in the solution will gain electrons and be reduced to elemental metal. Due to the multiple negative electrode plates 4 being equidistantly distributed... The addition of a cloth significantly increases the reaction area, increasing the contact opportunities between precious metal ions and the negative electrode plate 4, thereby improving the reaction rate. Simultaneously, the stable electrode connection structure and the efficient power supply system of the battery cell 5 ensure stable current transmission, preventing a decrease in reaction efficiency due to current fluctuations. Under optimized electrolysis conditions with precise control of current intensity, electrolysis time, electrolyte composition, and concentration, precious metal ions can be preferentially reduced and deposited on the surface of the negative electrode metal rod 7. As the electrolysis process continues, a large amount of precious metal will rapidly deposit on the negative electrode plate 4. By periodically treating the negative electrode plate 4, the deposited precious metal can be collected, thus achieving the goal of efficiently extracting precious metals from solutions containing precious metal ions. This electrolyzer utilizes the principle of redox reactions during electrolysis, exhibiting outstanding efficiency and possessing significant application value in the field of precious metal recycling. It provides strong technical support for precious metal extraction operations, greatly improving production efficiency and resource recycling rates.

[0041] Reference Figures 1-4The bottom of the booster 9 is fixedly connected to the top rear left end of the carrier plate 1, which can compress external gas and provide a power source for the entire solution turbulence system. The output end of the booster 9 is fixedly connected to a pressure stabilizing tank 10, the bottom of which is fixedly connected to the top rear right end of the carrier plate 1. This pressure stabilizing tank 10 can stably store and regulate the pressure of the boosted gas, ensuring stable gas pressure output and avoiding adverse effects of pressure fluctuations on the electrolyte turbulence effect. A partition 11 is fixedly connected to the center of the inside of the pressure stabilizing tank 10, dividing the tank into different areas for gas processing at different pressures. A pressure regulator 12 is fixedly installed in the middle of the partition 11, which can accurately control the gas pressure balance between the high-pressure chamber 13 and the pressure stabilizing chamber 14, ensuring that the gas output pressure meets the requirements and facilitating uniform electrolyte turbulence. A high-pressure chamber 13 is set on the left side of the inside of the pressure stabilizing tank 10 to store high-pressure gas, providing a stable pressure output for the subsequent process. The pressure stabilizing tank 10 has a pressure stabilizing chamber 14 on its right side, which can stabilize the gas after it has been regulated by the pressure regulator 12, so that the output gas pressure is uniform and constant. The right end of the pressure stabilizing tank 10 is connected to a conduit 15, which is used to transport the stabilized gas to the diversion pipe 17. An electric control valve 16 is fixedly installed in the middle of the conduit 15, which can precisely control the gas flow according to the working requirements of the electrolyzer, thereby flexibly adjusting the turbulence intensity of the electrolyte. The output end of the conduit 15 is connected to the diversion pipe 17, which plays the role of gas diversion, so that the gas is evenly distributed to each nozzle 18. Multiple nozzles 18 are fixedly installed at equal intervals on the top of the diversion pipe 17. The tops of the multiple nozzles 18 penetrate the inner bottom wall of the electrolytic cell 2, which can spray the gas into the electrolyte in the electrolytic cell 2 in a specific form, forming a strong airflow disturbance, effectively improving the fluidity of the electrolyte and promoting its uniform distribution, thereby increasing the current density and optimizing the electrolysis reaction effect.

[0042] Specifically, the booster 9 in the solution turbulence mechanism compresses external gas during operation and delivers the compressed gas to the pressure stabilizing tank 10. The central partition 11 inside the pressure stabilizing tank 10 divides the tank into two parts: a high-pressure chamber 13 on the left and a pressure stabilizing chamber 14 on the right. A pressure regulator 12, fixedly installed in the middle of the partition 11, precisely controls the gas pressure balance between the high-pressure chamber 13 and the pressure stabilizing chamber 14, ensuring stable output gas pressure. When the booster 9 compresses and delivers gas to the high-pressure chamber 13 of the pressure stabilizing tank 10, the high-pressure gas, under the regulation of the pressure regulator 12, enters the pressure stabilizing chamber 14 at a stable pressure. The gas in the pressure stabilizing chamber 14 is transmitted through a conduit 15 connected to the right end. The electrically controlled valve 16 in the middle of the conduit 15 can precisely control the gas flow rate according to the working requirements of the electrolyzer. When the electrically controlled valve 16 is opened, the gas enters the diversion pipe 17 along the conduit 15. The top of the diversion pipe 17... Multiple nozzles 18 are installed at a distance, with their tops penetrating the inner bottom wall of the electrolytic cell 2. High-pressure gas ejected from the nozzles 18 rises rapidly at the bottom of the electrolytic cell 2, creating airflow disturbance in the electrolyte. This airflow disturbance effectively enhances the fluidity of the electrolyte, allowing it to churn fully within the electrolytic cell 2. Under the impact of the gas, the electrolyte, which was originally in a relatively static or slow-flowing state, is rapidly mixed and circulated, thus achieving a uniform distribution of the electrolyte. In a uniform electrolyte environment, current can be conducted more smoothly between the positive electrode 3 and the negative electrode 4, reducing current conduction obstacles caused by uneven electrolyte concentration or local stagnation. This allows a larger current to pass through the electrode per unit area, thereby increasing the current density. A higher current density helps to accelerate the electrolysis reaction rate, significantly increasing the deposition rate of precious metal ions on the electrodes, and further improving the efficiency of the electrolytic machine in extracting precious metals.

[0043] Reference Figure 1 and Figure 2A mounting frame 19 is fixedly connected to the top left side of the carrier plate 1. The mounting frame 19 provides a stable installation position for the crusher 20, ensuring that the crusher 20 will not shake or shift during operation. The crusher 20 is fixedly installed inside the mounting frame 19, which can crush the raw materials that need to be electrolyzed, crushing large pieces of material into small particles or powder, increasing the contact area between the material and the electrolyte, and improving the extraction efficiency of precious metals. A control console 21 is fixedly connected to the front right end of the electrolytic cell 2. The control console 21 serves as the core control hub of the entire electrolytic machine and can regulate the operating status of the electrolytic machine. Multiple control buttons 22 are fixedly connected to the top of the control console 21. These control buttons 22 can realize the operation control of different functions of the electrolytic machine to meet different work requirements. A voltmeter 23 is fixedly connected to the front middle of the electrolytic cell 2. The voltmeter 23 is electrically connected to the positive electrode conductive plate 3 and can monitor the voltage across the positive electrode conductive plate 3 in real time, allowing the operator to understand the voltage status of the electrolytic reaction in a timely manner, so as to take measures to adjust quickly when the voltage is abnormal, and ensure that the electrolysis process is stable and safe.

[0044] Specifically, the crusher 20 inside the mounting frame 19 can compress larger pieces of material into smaller pieces, increasing the surface area of ​​the material so that it can come into more full contact with the electrolyte when it enters the electrolytic cell 2 for electrolysis, thereby improving the efficiency of precious metal extraction. The control console 21 is the control center of the entire electrolytic machine. The control button 22 on its top is used to adjust the current intensity during the electrolysis process. By changing the current magnitude, the rate of electrolysis reaction is controlled. The voltmeter 23 can monitor the voltage across the positive electrode conductive plate 3 in the electrolysis process in the electrolytic cell 2 in real time. The value displayed by the voltmeter 23 can be used to intuitively understand the current voltage status of the electrolysis reaction so as to detect abnormal voltage conditions in a timely manner.

[0045] Reference Figure 1 , Figure 3 and Figure 5 The bottom right side of the electrolytic cell 2 is connected to a drain pipe 24, which can drain the electrolyte in the electrolytic cell 2 when needed, facilitating electrolyte replacement or cleaning. A valve 25 is fixedly installed on the top of the drain pipe 24. The valve 25 can precisely control the discharge flow and start / stop of the electrolyte, ensuring the convenience and controllability of electrolyte discharge operation. A placement rack 26 is fixedly installed in the lower middle part of the inner wall of the electrolytic cell 2. The placement rack 26 is made of non-conductive material and can provide a safe placement platform for some auxiliary electrolysis items or monitoring equipment, avoiding short circuits caused by contact with the electrodes. The tops of multiple negative electrode metal rods 7 are fixedly connected to extraction rings 27. The extraction rings 27 can be used to collect the precious metals deposited in the negative electrode area after the electrolysis reaction, facilitating subsequent precious metal extraction operations.

[0046] Specifically, the drain pipe 24 can drain the electrolyte in the electrolytic cell 2 when needed. The opening of the top regulating valve 25 can precisely control the speed of electrolyte drainage to meet different operational needs. The placement rack 26 is fixedly installed in the lower part of the inner wall of the electrolytic cell 2 and is made of non-conductive material, which can effectively prevent short circuits between the items placed on it and the electrodes, ensuring the safe operation of the electrolytic machine and the normal progress of the electrolytic reaction. The extraction ring 27 can easily pick up the negative electrode metal rod 7, improving the convenience and efficiency of precious metal extraction.

[0047] Working Principle: The electrolytic cell 2 at the top of the carrier plate 1 is the core container for the electrolytic reaction. The positive conductive plate 3, fixedly connected to the rear side inside the electrolytic cell 2, becomes the anode after energization, undergoing an oxidation reaction. Multiple negative electrode plates 4 are equidistantly connected to the top front side of the electrolytic cell 2. The battery cells 5, fixedly connected to the bottom front of these negative electrode plates 4, primarily provide electrical energy, forming a closed loop in the entire electrolysis system. When the circuit is connected, the current is conducted to the negative electrode plates 4 through the negative electrode metal rod 7. The negative electrode metal rod 7 passes through the mounting groove 6 at the rear top of the negative electrode plate 4 and is engaged with the mounting groove 6 by a fixed circular plate 8, thus achieving a stable connection and ensuring that the current can smoothly travel from the battery cell 5 through the negative electrode metal rod 7 to the negative electrode plate 4. In the electrolyte containing precious metal ions, after energization, the positive conductive plate 3 at the anode undergoes an oxidation reaction, causing the metal ions to lose their... The noble metal ions in the solution lose electrons and dissolve into the electrolyte. At the cathode, i.e., the negative electrode plate 4, the noble metal ions in the solution gain electrons and are reduced to elemental metals. Due to the equidistant distribution of multiple negative electrode plates 4, the reaction area is greatly increased, which increases the contact opportunities between the noble metal ions and the negative electrode plate 4, thereby improving the reaction rate. At the same time, the stable electrode connection structure and the efficient power supply system of the battery cell 5 ensure stable current transmission and avoid the reduction of reaction efficiency caused by current fluctuations. Under the optimized electrolysis conditions of precise control of current intensity, electrolysis time, electrolyte composition and concentration, noble metal ions can be efficiently promoted to be preferentially reduced and deposited on the surface of the negative electrode metal rod 7. As the electrolysis process continues, a large amount of noble metal will be rapidly deposited on the negative electrode plate 4. By periodically treating the negative electrode plate 4, the deposited noble metal can be collected.

[0048] Furthermore, the booster compressor 9 compresses external gas during operation and delivers it to the pressure stabilizing tank 10. The pressure stabilizing tank 10 is divided into two parts by a central partition 11: a high-pressure chamber 13 on the left and a pressure stabilizing chamber 14 on the right. A pressure regulator 12, fixedly installed in the middle of the partition 11, precisely controls the gas pressure balance between the high-pressure chamber 13 and the pressure stabilizing chamber 14, ensuring stable output gas pressure. After the booster compressor 9 compresses and delivers gas to the high-pressure chamber 13 of the pressure stabilizing tank 10, the high-pressure gas enters the pressure stabilizing chamber 14 at a stable pressure under the regulation of the pressure regulator 12. The gas in the pressure stabilizing chamber 14 is transmitted through a conduit 15 connected to the right end. The electrically controlled valve 16 in the middle of the conduit 15 can precisely control the gas flow according to the operating requirements of the electrolyzer. When the solenoid valve 16 is opened, the gas enters the diversion pipe 17 along the conduit 15. Multiple nozzles 18 are equidistantly installed at the top of the diversion pipe 17, and their tops penetrate the inner bottom wall of the electrolytic cell 2. The high-pressure gas ejected from the nozzles 18 rises rapidly at the bottom of the electrolytic cell 2, forming airflow disturbance in the electrolyte. This airflow disturbance can effectively improve the fluidity of the electrolyte, allowing the electrolyte to churn fully within the electrolytic cell 2. Under the impact of the gas, the electrolyte, which was originally in a relatively static or slow-flowing state, is rapidly mixed and circulated, thereby achieving a uniform distribution of the electrolyte. In a uniform electrolyte environment, the current can be conducted more smoothly between the positive electrode conductive plate 3 and the negative electrode plate 4, reducing the current conduction obstacles caused by uneven electrolyte concentration or local stagnation.

[0049] Finally, it should be noted that the above description is only a preferred embodiment of the present utility model and is not intended to limit the present utility model. Although the present utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.

Claims

1. An electrolysis machine, comprising a carrier plate (1), characterized in that: An electrolytic cell (2) is fixedly connected to the top front side of the carrier plate (1). A positive electrode conductive plate (3) is fixedly connected to the inner rear side of the electrolytic cell (2). Multiple negative electrode plates (4) are equidistantly penetrating the top front side of the electrolytic cell (2). A battery cell (5) is fixedly connected to the bottom front end of each of the multiple negative electrode plates (4). An installation groove (6) is opened on the top rear side of each of the multiple negative electrode plates (4). A negative electrode metal rod (7) is penetrating inside each of the multiple installation grooves (6). A fixing circular plate (8) is fixedly connected to the middle and upper part of each of the multiple negative electrode metal rods (7). The multiple fixing circular plates (8) are respectively engaged with the multiple installation grooves (6). A solution tumbling mechanism is provided on the top rear side of the carrier plate (1).

2. An electrolysis machine according to claim 1, characterized in that: The solution turbulence mechanism includes a booster (9), the bottom of which is fixedly connected to the left rear end of the top of the carrier plate (1). A pressure stabilizing tank (10) is fixedly connected to the output end of the booster (9). The bottom of the pressure stabilizing tank (10) is fixedly connected to the right rear end of the top of the carrier plate (1). A partition (11) is fixedly connected to the center of the interior of the pressure stabilizing tank (10). A pressure regulator (12) is fixedly installed in the middle of the partition (11). The interior of the pressure stabilizing tank (10)... A high-pressure chamber (13) is provided on the left side, and a pressure stabilizing chamber (14) is provided on the right side inside the pressure stabilizing tank (10). A conduit (15) is connected to the right end of the pressure stabilizing tank (10). An electric control valve (16) is fixedly installed in the middle of the conduit (15). A diversion pipe (17) is connected to the output end of the conduit (15). Multiple nozzles (18) are fixedly installed at equal intervals on the top of the diversion pipe (17). The tops of the multiple nozzles (18) penetrate the inner bottom wall of the electrolytic cell (2).

3. An electrolysis machine according to claim 1, characterized in that: A mounting bracket (19) is fixedly connected to the top left side of the carrier plate (1), and a crusher (20) is fixedly installed inside the mounting bracket (19).

4. An electrolysis machine according to claim 1, characterized in that: A control console (21) is fixedly connected to the front right end of the electrolytic cell (2), and multiple control buttons (22) are fixedly connected to the top of the control console (21).

5. An electrolysis machine according to claim 1, characterized in that: A voltmeter (23) is fixedly connected to the middle of the front side of the electrolytic cell (2), and the voltmeter (23) is electrically connected to the positive electrode conductive plate (3).

6. An electrolysis machine according to claim 1, characterized in that: The bottom right side of the electrolytic cell (2) is connected to a drain pipe (24), and a valve (25) is fixedly installed on the top of the drain pipe (24).

7. An electrolysis machine according to claim 1, characterized in that: A placement rack (26) is fixedly installed on the lower part of the inner wall of the electrolytic cell (2), and the placement rack (26) is made of non-conductive material.

8. An electrolysis machine according to claim 1, characterized in that: Each of the multiple negative electrode metal rods (7) has an extraction ring (27) fixedly connected to its top, and the exterior of each of the multiple extraction rings (27) is treated with a frosting process.

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